US2618935A - Apparatus for vaporizing hydrocarbons - Google Patents

Apparatus for vaporizing hydrocarbons Download PDF

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US2618935A
US2618935A US210012A US21001251A US2618935A US 2618935 A US2618935 A US 2618935A US 210012 A US210012 A US 210012A US 21001251 A US21001251 A US 21001251A US 2618935 A US2618935 A US 2618935A
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valve
pressure
chamber
tank
open
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Jr Joseph J Malir
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    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23K—FEEDING FUEL TO COMBUSTION APPARATUS
    • F23K5/00—Feeding or distributing other fuel to combustion apparatus
    • F23K5/02—Liquid fuel
    • F23K5/14—Details thereof
    • F23K5/22—Vaporising devices
    • 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
    • F17C2205/00—Vessel construction, in particular mounting arrangements, attachments or identifications means
    • F17C2205/03—Fluid connections, filters, valves, closure means or other attachments
    • F17C2205/0302—Fittings, valves, filters, or components in connection with the gas storage device
    • F17C2205/0323—Valves
    • F17C2205/0326—Valves electrically actuated
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2205/00—Vessel construction, in particular mounting arrangements, attachments or identifications means
    • F17C2205/03—Fluid connections, filters, valves, closure means or other attachments
    • F17C2205/0302—Fittings, valves, filters, or components in connection with the gas storage device
    • F17C2205/0323—Valves
    • F17C2205/0332—Safety valves or pressure relief valves
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • 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
    • F17C2205/0335—Check-valves or non-return 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
    • F17C2205/0338—Pressure regulators
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2221/00—Handled fluid, in particular type of fluid
    • F17C2221/03—Mixtures
    • F17C2221/032—Hydrocarbons
    • F17C2221/035—Propane butane, e.g. LPG, GPL
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2223/00—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
    • F17C2223/01—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the phase
    • F17C2223/0146—Two-phase
    • F17C2223/0153—Liquefied gas, e.g. LPG, GPL
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2223/00—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
    • F17C2223/03—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the pressure level
    • F17C2223/033—Small pressure, e.g. for liquefied 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
    • 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
    • F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
    • F17C2227/03—Heat exchange with the fluid
    • F17C2227/0302—Heat exchange with the fluid by heating
    • F17C2227/0306—Heat exchange with the fluid by heating using the same fluid
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
    • F17C2227/03—Heat exchange with the fluid
    • F17C2227/0302—Heat exchange with the fluid by heating
    • F17C2227/0309—Heat exchange with the fluid by heating using another fluid
    • F17C2227/0316—Water heating
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
    • F17C2227/03—Heat exchange with the fluid
    • F17C2227/0302—Heat exchange with the fluid by heating
    • F17C2227/0309—Heat exchange with the fluid by heating using another fluid
    • F17C2227/0323—Heat exchange with the fluid by heating using another fluid in a closed loop
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
    • F17C2227/03—Heat exchange with the fluid
    • F17C2227/0302—Heat exchange with the fluid by heating
    • F17C2227/0332—Heat exchange with the fluid by heating by burning a combustible
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2250/00—Accessories; Control means; Indicating, measuring or monitoring of parameters
    • F17C2250/04—Indicating or measuring of parameters as input values
    • F17C2250/0404—Parameters indicated or measured
    • F17C2250/0408—Level of content in the vessel
    • F17C2250/0413—Level of content in the vessel with floats
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2250/00—Accessories; Control means; Indicating, measuring or monitoring of parameters
    • F17C2250/04—Indicating or measuring of parameters as input values
    • F17C2250/0404—Parameters indicated or measured
    • F17C2250/043—Pressure
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2250/00—Accessories; Control means; Indicating, measuring or monitoring of parameters
    • F17C2250/07—Actions triggered by measured parameters
    • F17C2250/072—Action when predefined value is reached
    • 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
    • F17C2265/00—Effects achieved by gas storage or gas handling
    • F17C2265/05—Regasification

Definitions

  • This invention relates to improvements in methods and apparatus for vaporizing hydrocarbons.
  • Another object is to provide apparatus of the foregoing type which embodies certain safety devices.
  • Another object is to vaporize hydrocarbons with novel heat exchanger apparatus which is supplied with heat by burning a portion of the vaporized hydrocarbon.
  • a hydrocarbon tank l0 which may be any shape, is provided with a filler pipe ll, having a conventional filler valve I2 at the exposed end thereof, and vapor return pipes 13, I4, the latter being provided with a similar valve I5.
  • the tank contains butane, pentane, propane, or any mixture of the foregoing or similar hydrocarbons.
  • a hose is connected between the supply of liquid hydrocarbon and valve 1'2, and a similar hose is connected between the space above the supply and valve 15 to permit the vapor above the liquid in tank It! to return to the supply, as well understood in the art.
  • an air compressor I6 is provided, this being driven by a suitable electric motor I! by-means of belt 18 or other power transmission means.
  • the compressor when in operation, delivers air through pipe [9, check valve 20, pipe 2
  • a branch pipe 23 having a check valve 24 therein connects pipe 2
  • a pressure responsive gauge and electric switch device 25 is connected to the tank by a pipe 26, the switch being adapted to close when the pressure in the tank falls below a predetermined value and to open when the pressure rises to another predetermined value. Details of this device have been omitted since there are various commercially available types, well known in the art, and no novelty is predicated on this device per se.
  • the switch and motor are electrically connected in series to electric lines LI, L2, and it will be apparent that the compressor auto matically maintains the pressure in tank, 10 between the predetermined values previously referred to.
  • the heat exchanger apparatus 30 comprises a tube 3
  • Upstanding pipe 33 contains air and forms an expansion chamber for the liquid in the jacket.
  • a pipe 34 is connected to the expansion chamber and is provided with a closure member 35 which may be removed to fill the jacket.
  • a safety blow-off valve 36 is connected to the 6X1 pansion chamber and is adapted to release excess pressure in the jacket in event certain of the controls should fail to function properly. Safety valves of this type are well known and hence details thereof are omitted to simplify the disclosure.
  • Liquid hydrocarbon from tank IE1 passes through foot check valve 31, pipe 38, check valve- 39, valve 40 operated by solenoid 40a, and into chamber 3 la.
  • Solenoid operated valve 40 is controlled by a liquid level responsive switch device 4 I operated by a float device 4 l a, the switch device closing when the liquid level in chamber 31a falls below a predetermined level and opening when it rises to the predetermined level, thus maintaining a substantially predetermined liquid level in chamber am.
  • a jacket temperature responsive switch device 42 is Wired in series with the level responsive switch, this switch opening upon a jacket temperature drop and, closing upon a jacket temperature rise. It is apparent, therefore, that if the jacket temperature falls below a predetermined value valve M) will not open, but when the jacket temperature rises to a predetermined value valve 40 may open if the liquid level responsive means calls for addition of liquid to chamber 31a.
  • a discharge vapor pipe 43 is connected to the other end of chamber 31a and is provided with a shut-oil valve 44. This pipe connects with a mixing or carbureting chamber 45 having an air supply pipe 46 and a discharge pipe 41.
  • the carbureting portion of the system may be ofdifferent forms, one of which is disclosed in detail in my copending application, Serial No. 210,011, filed on February 8, 1951, concurrently with this application.
  • a branch pipe 48 connects with pipe 43; and is provided with a conventional pressure reducing device 49, which will maintain the preslator 49.
  • Thermocouple means 55 is disposed in the flame of the pilot light and provides a source of electric current for operating solenoid 50a.
  • a pressure responsive switch device 66 is connected to pipe 43, the switch being normally closed but adapted to open if the pressure in pipe 43 ex-' ceeds a predetermined value.
  • a temperature responsive switch device 56 similar to 42, is connected to the jacket.
  • a conduit 5'! communicates with chamber 3m and tank 20, this conduit being provided with a check valve 58 and a valve 59 adapted to open when the pressure in chamber 31a exceeds the pressure'in tank [0 by a desired differential, the latter being adjustable by a movable actuator 60 adapted to vary the pressure of spring 61 engaging valve 59.
  • the switch in temperature responsive device 56 closes and a circuit is established from one terminal of thermocouple device 55, through wire. 62, solenoid 50a, wire 63, temperature responsive switch device 56,,wire 64, pressureresponsive switch device 66, and to the other terminal of the thermocouple device through wire 65.
  • valve 50 is open and liquid hydrocarbon is delivered to jets 52 which are lighted by pilot light 53.
  • the switch in temperature responsive device 56 opens the circuit and permits. valve 50 to close, thus discontinuing the addition of heat to the heat exchanger. In thevoperation just described, the switch of pressure responsive device 66- normally remains closed.
  • temperature responsive device 56 should fail to open the circuit when the heat exchanger reached the higher predetermined temperature, it is apparent that the temperature would continue to rise. This, however, would increase the pressure in chamber 43 and after it has increased to a certain value, the switch of pressure responsive device 66 will open, thus opening the circuit and permitting valve 53 to close, discontinuing the addition of heat to the heat exchanger. It will be apparent that under normal conditions there will be a closed circuit through pressure responsive switch device 66 but if the pressure in the heat exchanger should exceed a predetermined value, switch 66 serves as a safety device to ensure-that the burner will be shut off. During normal operation, valve 59 will be closed. If for any reason, however, pressure in chamber 3Ia exceeds a certain predetermined value above tank pressure, this valve will open and permit hydrocarbon to return to tank I0, thus relieving the pressure in chamber 3 I a. 7
  • Valve 24 serves as a safety means for preventing liquid hydrocarbon from flowing from the tank to the compressor in event valve 20 should leak.
  • will balance the pressure of the liquid in conduit 22. If valve 20 should now leak, the pressure of liquid in conduit 22 will exceed the air pressure and the liquid will rise in conduit 22; after it rises to some extent, the pressure in the space above the tank will exceed the pressure in conduit 2! and open valve 24. Any leakage thereafter, past valve 20 will be vapor leakage rather than liquid leakage.
  • Apparatus for vaporizing liquid hydrocarbons comprising a tank for containing the hydrocarbon, means for intermittently delivering air to the tank and for automatically maintaining a hydrocarbon therein between predetermined limits of pressure, a heat exchanger having a closed vaporizing chamber, a conduit for delivering liquid hydrocarbon from the tank to the chamber, a valve in the conduit adapted to open or close to permit or prevent flow of liquid therethrough, first electric means for operating the valve, chamber temperature and liquid level responsive switches and an electric circuit including same and said first electric means adapted to open the valve when the temperature in the chamber rises to a predetermined limit and the liquid level falls below a predetermined level and to close the valve when the liquid level rises to said predetermined level, means for heating the chamber comprising a main burner adapted to burn a portion of the vaporized hydrocarbon, a valve adapted to open or close to permit or pre vent supply of vapor to the main burner, second electric means for operating the last named valve, 2.
  • thermocouple heated by the pilot burner, a temperature responsive switch and an electric circuit including the thermocouple and second electric means adapted to open the second named valve when the temperature in the chamber falls to a predetermined limit and to close the second named valve when the temperature in the chamber rises to another predetermined limit.
  • Apparatus in accordance with claim 1 including a normally closed pressure responsive switch in the last named circuit adapted to open when the pressure in the chamber rises to a predetermined limit. 7
  • Apparatus in accordance with claim .1 including a conduit communicating the tank with said chamber, and valve means in the last named conduit adapted to open when the pressure in said chamber exceeds, by a predetermined amount, the pressure in the tank.
  • Apparatus in accordance with claim 1 including a normally closed pressure responsive switch in the last named circuit adapted to open when the pressure in the chamber rises to a predetermined limit, a conduit communicating the tank'with said chamber, and valve means in the last named conduit adapted to open when the pressure in said chamber exceeds, by a predetermined amount, the pressure in the tank.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)

Description

Patented Nov. 25, 1952 APPARATUS FOR VAPORIZING HYDROCARBONS Joseph J. Malir, Jr., Denver, Colo.
Application February 8, 1951, Serial No. 210,012
4 Claims.
This invention relates to improvements in methods and apparatus for vaporizing hydrocarbons.
Among the objects of the invention are the provision of improved methods and apparatus for automatically vaporizing hydrocarbons.
Another object is to provide apparatus of the foregoing type which embodies certain safety devices.
Another object is to vaporize hydrocarbons with novel heat exchanger apparatus which is supplied with heat by burning a portion of the vaporized hydrocarbon.
Still further objects, advantages, and salient features will become apparent from the description to follow, the appended claims, and the accompanying drawing in which:
The single figure diagrammatically illustrates apparatus and a system, portions being shown in section and other portions being broken away, with which the method of vaporizing hydrocarbons may be practised.
Referring in detail to the drawing, a hydrocarbon tank l0, which may be any shape, is provided with a filler pipe ll, having a conventional filler valve I2 at the exposed end thereof, and vapor return pipes 13, I4, the latter being provided with a similar valve I5. The tank contains butane, pentane, propane, or any mixture of the foregoing or similar hydrocarbons. When it is desired to fill the tank, a hose is connected between the supply of liquid hydrocarbon and valve 1'2, and a similar hose is connected between the space above the supply and valve 15 to permit the vapor above the liquid in tank It! to return to the supply, as well understood in the art.
To maintain the hydrocarbon in the tank under pressure an air compressor I6 is provided, this being driven by a suitable electric motor I! by-means of belt 18 or other power transmission means. The compressor, when in operation, delivers air through pipe [9, check valve 20, pipe 2| and pipe 22. A branch pipe 23 having a check valve 24 therein connects pipe 2| and the space above the liquid in tank I D.
,,A pressure responsive gauge and electric switch device 25 is connected to the tank by a pipe 26, the switch being adapted to close when the pressure in the tank falls below a predetermined value and to open when the pressure rises to another predetermined value. Details of this device have been omitted since there are various commercially available types, well known in the art, and no novelty is predicated on this device per se. The switch and motor are electrically connected in series to electric lines LI, L2, and it will be apparent that the compressor auto matically maintains the pressure in tank, 10 between the predetermined values previously referred to.
The heat exchanger apparatus 30 comprises a tube 3|, closed at its ends, providing a vaporizing chamber 3Ia., and a surrounding spaced tube 32, also similarly closed, to provide a jacket for receiving a suitable heat exchange liquid, such as.
water. Upstanding pipe 33 contains air and forms an expansion chamber for the liquid in the jacket. A pipe 34 is connected to the expansion chamber and is provided with a closure member 35 which may be removed to fill the jacket. A safety blow-off valve 36 is connected to the 6X1 pansion chamber and is adapted to release excess pressure in the jacket in event certain of the controls should fail to function properly. Safety valves of this type are well known and hence details thereof are omitted to simplify the disclosure.
Liquid hydrocarbon from tank IE1 passes through foot check valve 31, pipe 38, check valve- 39, valve 40 operated by solenoid 40a, and into chamber 3 la. Solenoid operated valve 40 is controlled by a liquid level responsive switch device 4 I operated by a float device 4 l a, the switch device closing when the liquid level in chamber 31a falls below a predetermined level and opening when it rises to the predetermined level, thus maintaining a substantially predetermined liquid level in chamber am. A jacket temperature responsive switch device 42 is Wired in series with the level responsive switch, this switch opening upon a jacket temperature drop and, closing upon a jacket temperature rise. It is apparent, therefore, that if the jacket temperature falls below a predetermined value valve M) will not open, but when the jacket temperature rises to a predetermined value valve 40 may open if the liquid level responsive means calls for addition of liquid to chamber 31a.
A discharge vapor pipe 43 is connected to the other end of chamber 31a and is provided with a shut-oil valve 44. This pipe connects with a mixing or carbureting chamber 45 having an air supply pipe 46 and a discharge pipe 41. The carbureting portion of the system may be ofdifferent forms, one of which is disclosed in detail in my copending application, Serial No. 210,011, filed on February 8, 1951, concurrently with this application. A branch pipe 48 connects with pipe 43; and is provided with a conventional pressure reducing device 49, which will maintain the preslator 49. Thermocouple means 55 is disposed in the flame of the pilot light and provides a source of electric current for operating solenoid 50a. A pressure responsive switch device 66 is connected to pipe 43, the switch being normally closed but adapted to open if the pressure in pipe 43 ex-' ceeds a predetermined value. A temperature responsive switch device 56, similar to 42, is connected to the jacket.
A conduit 5'! communicates with chamber 3m and tank 20, this conduit being provided with a check valve 58 and a valve 59 adapted to open when the pressure in chamber 31a exceeds the pressure'in tank [0 by a desired differential, the latter being adjustable by a movable actuator 60 adapted to vary the pressure of spring 61 engaging valve 59.
Assuming that the-jacket temperature of the heat exchanger has fallen to a certain predetermined value, the switch in temperature responsive device 56 closes and a circuit is established from one terminal of thermocouple device 55, through wire. 62, solenoid 50a, wire 63, temperature responsive switch device 56,,wire 64, pressureresponsive switch device 66, and to the other terminal of the thermocouple device through wire 65. When this circuit is established, valve 50 is open and liquid hydrocarbon is delivered to jets 52 which are lighted by pilot light 53. When the temperature rises to a higher predetermined value, the switch in temperature responsive device 56 opens the circuit and permits. valve 50 to close, thus discontinuing the addition of heat to the heat exchanger. In thevoperation just described, the switch of pressure responsive device 66- normally remains closed. If, however, temperature responsive device 56 should fail to open the circuit when the heat exchanger reached the higher predetermined temperature, it is apparent that the temperature would continue to rise. This, however, would increase the pressure in chamber 43 and after it has increased to a certain value, the switch of pressure responsive device 66 will open, thus opening the circuit and permitting valve 53 to close, discontinuing the addition of heat to the heat exchanger. It will be apparent that under normal conditions there will be a closed circuit through pressure responsive switch device 66 but if the pressure in the heat exchanger should exceed a predetermined value, switch 66 serves as a safety device to ensure-that the burner will be shut off. During normal operation, valve 59 will be closed. If for any reason, however, pressure in chamber 3Ia exceeds a certain predetermined value above tank pressure, this valve will open and permit hydrocarbon to return to tank I0, thus relieving the pressure in chamber 3 I a. 7
Valve 24, previously referred to, serves as a safety means for preventing liquid hydrocarbon from flowing from the tank to the compressor in event valve 20 should leak. When the compressor ceases operation (valve 24 being closed), the pressure in conduit 2| will balance the pressure of the liquid in conduit 22. If valve 20 should now leak, the pressure of liquid in conduit 22 will exceed the air pressure and the liquid will rise in conduit 22; after it rises to some extent, the pressure in the space above the tank will exceed the pressure in conduit 2! and open valve 24. Any leakage thereafter, past valve 20 will be vapor leakage rather than liquid leakage.
Having described the invention, what is claimed as new is:
1. Apparatus for vaporizing liquid hydrocarbons, comprising a tank for containing the hydrocarbon, means for intermittently delivering air to the tank and for automatically maintaining a hydrocarbon therein between predetermined limits of pressure, a heat exchanger having a closed vaporizing chamber, a conduit for delivering liquid hydrocarbon from the tank to the chamber, a valve in the conduit adapted to open or close to permit or prevent flow of liquid therethrough, first electric means for operating the valve, chamber temperature and liquid level responsive switches and an electric circuit including same and said first electric means adapted to open the valve when the temperature in the chamber rises to a predetermined limit and the liquid level falls below a predetermined level and to close the valve when the liquid level rises to said predetermined level, means for heating the chamber comprising a main burner adapted to burn a portion of the vaporized hydrocarbon, a valve adapted to open or close to permit or pre vent supply of vapor to the main burner, second electric means for operating the last named valve, 2. pilot burner, a thermocouple heated by the pilot burner, a temperature responsive switch and an electric circuit including the thermocouple and second electric means adapted to open the second named valve when the temperature in the chamber falls to a predetermined limit and to close the second named valve when the temperature in the chamber rises to another predetermined limit.
2. Apparatus in accordance with claim 1 including a normally closed pressure responsive switch in the last named circuit adapted to open when the pressure in the chamber rises to a predetermined limit. 7
3. Apparatus in accordance with claim .1 including a conduit communicating the tank with said chamber, and valve means in the last named conduit adapted to open when the pressure in said chamber exceeds, by a predetermined amount, the pressure in the tank.
4. Apparatus in accordance with claim 1 including a normally closed pressure responsive switch in the last named circuit adapted to open when the pressure in the chamber rises to a predetermined limit, a conduit communicating the tank'with said chamber, and valve means in the last named conduit adapted to open when the pressure in said chamber exceeds, by a predetermined amount, the pressure in the tank.
JOSEPH JLMALIR, JR.
REFERENCES CITED The following references are of record in the file of this patent:
UNITED STATES PATENTS
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Cited By (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2698055A (en) * 1952-01-02 1954-12-28 Neill Tank Company Inc O Gas generator for oil well pump engines
US2728329A (en) * 1951-12-17 1955-12-27 Gas Systems Inc Liquid heating system and control therefor
US2731801A (en) * 1956-01-24 Relief valve for vaporizer
US2761286A (en) * 1955-03-18 1956-09-04 Gaines H Billue Vaporizer for liquid petroleum supply tanks
US2788779A (en) * 1953-12-14 1957-04-16 Phillips Petroleum Co Liquefied petroleum gas system
US2827782A (en) * 1952-12-16 1958-03-25 Brown & Bigelow Liquefied petroleum gas lighter
US2856944A (en) * 1953-10-28 1958-10-21 Constock Liquid Methane Corp Means for controlling the pressure in an insulated tank containing liquefied methane
US2884943A (en) * 1954-04-22 1959-05-05 Bendix Aviat Corp Liquid-gas converter system
US2922289A (en) * 1956-08-27 1960-01-26 Mitchell Co John E Liquid petroleum gas vaporizer system
US2996893A (en) * 1958-07-03 1961-08-22 Santa Barbara Res Ct Low temperature liquid transfer apparatus
US3054270A (en) * 1960-08-19 1962-09-18 American Sterilizer Co Gas sterilizing system
US3319435A (en) * 1966-03-28 1967-05-16 John A Boyd Liquefied petroleum gas vaporization system
US3407787A (en) * 1967-01-03 1968-10-29 Ransome Torck & Burner Co Lpg vaporizer
US3451225A (en) * 1968-02-08 1969-06-24 Daryl G Hill Water-jacket warmer for stationary fuel tank
US3712073A (en) * 1971-02-03 1973-01-23 Black Sivalls & Bryson Inc Method and apparatus for vaporizing and superheating cryogenic fluid liquids
US3883322A (en) * 1973-08-23 1975-05-13 Jr Henry W Bivins Blending apparatus for vaporizing propane
US4063871A (en) * 1975-07-22 1977-12-20 Societe Anonyme Automobiles Citroen Boiler burners
FR2706580A1 (en) * 1993-06-17 1994-12-23 Butagaz Vapourising unit for LPG tank and LPG tank equipped with such a unit
WO1996029543A1 (en) * 1995-03-23 1996-09-26 Avneri, Jonathan Pressurizer for burner fuel container

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US1046539A (en) * 1912-05-04 1912-12-10 Power Plant Engineering Co Generating oil-gas for explosive-engines.
US1337108A (en) * 1917-02-09 1920-04-13 John J Weithaus Liquid-hydrocarbon-vapor producer
US1960108A (en) * 1931-01-02 1934-05-22 S H G Inc Apparatus for generating combustible gas
US2329750A (en) * 1940-11-18 1943-09-21 Bryce R Sprayberry Fuel gas vaporizer
US2493369A (en) * 1945-04-03 1950-01-03 American Liquid Gas Corp Hydrocarbon fuel vaporizer

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1046539A (en) * 1912-05-04 1912-12-10 Power Plant Engineering Co Generating oil-gas for explosive-engines.
US1337108A (en) * 1917-02-09 1920-04-13 John J Weithaus Liquid-hydrocarbon-vapor producer
US1960108A (en) * 1931-01-02 1934-05-22 S H G Inc Apparatus for generating combustible gas
US2329750A (en) * 1940-11-18 1943-09-21 Bryce R Sprayberry Fuel gas vaporizer
US2493369A (en) * 1945-04-03 1950-01-03 American Liquid Gas Corp Hydrocarbon fuel vaporizer

Cited By (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2731801A (en) * 1956-01-24 Relief valve for vaporizer
US2728329A (en) * 1951-12-17 1955-12-27 Gas Systems Inc Liquid heating system and control therefor
US2698055A (en) * 1952-01-02 1954-12-28 Neill Tank Company Inc O Gas generator for oil well pump engines
US2827782A (en) * 1952-12-16 1958-03-25 Brown & Bigelow Liquefied petroleum gas lighter
US2856944A (en) * 1953-10-28 1958-10-21 Constock Liquid Methane Corp Means for controlling the pressure in an insulated tank containing liquefied methane
US2788779A (en) * 1953-12-14 1957-04-16 Phillips Petroleum Co Liquefied petroleum gas system
US2884943A (en) * 1954-04-22 1959-05-05 Bendix Aviat Corp Liquid-gas converter system
US2761286A (en) * 1955-03-18 1956-09-04 Gaines H Billue Vaporizer for liquid petroleum supply tanks
US2922289A (en) * 1956-08-27 1960-01-26 Mitchell Co John E Liquid petroleum gas vaporizer system
US2996893A (en) * 1958-07-03 1961-08-22 Santa Barbara Res Ct Low temperature liquid transfer apparatus
US3054270A (en) * 1960-08-19 1962-09-18 American Sterilizer Co Gas sterilizing system
US3319435A (en) * 1966-03-28 1967-05-16 John A Boyd Liquefied petroleum gas vaporization system
US3407787A (en) * 1967-01-03 1968-10-29 Ransome Torck & Burner Co Lpg vaporizer
US3451225A (en) * 1968-02-08 1969-06-24 Daryl G Hill Water-jacket warmer for stationary fuel tank
US3712073A (en) * 1971-02-03 1973-01-23 Black Sivalls & Bryson Inc Method and apparatus for vaporizing and superheating cryogenic fluid liquids
US3883322A (en) * 1973-08-23 1975-05-13 Jr Henry W Bivins Blending apparatus for vaporizing propane
US4063871A (en) * 1975-07-22 1977-12-20 Societe Anonyme Automobiles Citroen Boiler burners
FR2706580A1 (en) * 1993-06-17 1994-12-23 Butagaz Vapourising unit for LPG tank and LPG tank equipped with such a unit
WO1996029543A1 (en) * 1995-03-23 1996-09-26 Avneri, Jonathan Pressurizer for burner fuel container

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