Liquid and compressed natural gas dispensing system

• US 7,069,730 B2
• Filed: 09/02/2003
• Issued: 07/04/2006
• Est. Priority Date: 08/30/2002
• Status: Active Grant

• Current Assignee: Chart Incorporated (Chart Industries Incorporated)
• Original Assignee: Chart Incorporated (Chart Industries Incorporated)
• Inventors: Drube, Thomas K., Gamble, Jesse, Emmer, Claus D., Zelasko, Craig
• Primary Examiner(s): Doerrler, William C.
• Application Number:
  US10/654,289
• Publication Number:
  US 20050016185A1
• Time in Patent Office: 1,036 Days
• Field of Search: 62/501, 62/502, 62/451, 62/481, 141/11, 141/82
• US Class Current: 62/50.1
• CPC Class Codes: F17C 13/025 having the pressure as the parameter
• CPC Class Codes: F17C 13/026 having the temperature as the parameter
• CPC Class Codes: F17C 2205/0332 Safety valves or pressure relief valves
• CPC Class Codes: F17C 2221/033 Methane, e.g. natural gas, CNG, LNG, GNL, GNC, PLNG
• CPC Class Codes: F17C 2223/0161 cryogenic, e.g. LNG, GNL, PLNG
• CPC Class Codes: F17C 2223/033 Small pressure, e.g. for liquefied gas
• CPC Class Codes: F17C 2223/046 in the liquid
• CPC Class Codes: F17C 2225/0123 gaseous, e.g. CNG, GNC
• CPC Class Codes: F17C 2225/0161 cryogenic, e.g. LNG, GNL, PLNG
• CPC Class Codes: F17C 2225/033 Small pressure, e.g. for liquefied gas
• CPC Class Codes: F17C 2225/035 High pressure, i.e. between 10 and 80 bars
• CPC Class Codes: F17C 2225/036 Very high pressure, i.e. above 80 bars
• CPC Class Codes: F17C 2225/043 in the gas
• CPC Class Codes: F17C 2225/046 in the liquid
• CPC Class Codes: F17C 2225/047 with a dip tube
• CPC Class Codes: F17C 2227/0107 by pressurising the ullage
• CPC Class Codes: F17C 2227/0142 with specified pump type, e.g. piston or impulsive type
• CPC Class Codes: F17C 2227/0178 in the vessel
• CPC Class Codes: F17C 2227/0302 by heating
• CPC Class Codes: F17C 2227/0393 using a vaporiser
• CPC Class Codes: F17C 2227/043 : by pressure cascade
• CPC Class Codes: F17C 2250/01 : Intermediate tanks
• CPC Class Codes: F17C 2250/032 : using computers
• CPC Class Codes: F17C 2250/0408 : Level of content in the vessel
• CPC Class Codes: F17C 2250/043 : Pressure
• CPC Class Codes: F17C 2250/0439 : Temperature
• CPC Class Codes: F17C 2250/0443 : Flow or movement of content
• CPC Class Codes: F17C 2250/0452 : Concentration of a product
• CPC Class Codes: F17C 2260/025 : Reducing transfer time
• CPC Class Codes: F17C 2265/022 : identical fluid
• CPC Class Codes: F17C 2270/0139 : Fuel stations
• CPC Class Codes: F17C 2270/0168 : by vehicles
• CPC Class Codes: F17C 5/007 : for individual gas tanks or containers, e.g. in vehicles filling with liquid fuel not under pressure, B60S5/02, B67D7/00
• CPC Class Codes: F17C 5/02 : for filling with liquefied gases
• CPC Class Codes: F17C 5/06 : for filling with compressed gases
• CPC Class Codes: F17C 7/02 : Discharging liquefied gases
• CPC Class Codes: F17C 9/00 : Methods or apparatus for discharging liquefied or solidified gases from vessels not under pressure
• CPC Class Codes: F17C 9/02 : with change of state, e.g. vaporisation

Abstract

A system dispenses both liquid natural gas (LNG) and compressed natural gas (CNG). A bulk tank contains a supply of LNG which is pumped to a smaller storage tank. After the storage tank is refilled, LNG from the bulk tank is pumped to a vaporizer so that CNG is produced. The CNG may be routed to the LNG in the storage tank to condition it. It is also used to recharge a pressurizing cylinder that is placed in communication with the head space of the storage tank when it is desired to rapidly dispense LNG to a vehicle. A bank of cascaded storage cylinders alternatively may receive CNG from the vaporizer for later dispensing through the system CNG dispenser. The CNG from the vaporizer may also be dispensed directly via the system CNG dispenser.

Claims

1. A system for dispensing cryogenic fluids comprising:

a) a bulk tank containing a supply of cryogenic liquid;

b) a pump in communication with the bulk tank;

c) a storage tank selectively in communication with the bulk tank so as to receive cryogenic liquid therefrom;

d) a vaporizer selectively in communication with the pump, said vaporizer receiving cryogenic liquid from the bulk tank via the pump so that a cryogenic gas is produced and said vaporizer selectively communicating directly with the storage tank so as to condition the liquid therein;

e) a bank of cascaded storage cylinders selectively in communication with the vaporizer so as to receive gas therefrom for dispensing; and

f) a pressurizing cylinder separate and distinct from the bank of cascaded storage cylinders and selectively in communication with the vaporizer so as to receive cryogenic gas therefrom, said pressurizing cylinder pressurizing said storage tank with gas so that the liquid in the storage tank may be dispensed therefrom while gas is simultaneously dispensed from the bank of cascaded storage cylinders.

2. The system of claim 1 wherein the vaporizer communicates with the storage tank via a dip tube disposed within the liquid therein.

3. The system of claim 1 wherein the gas from the pressurizing cylinder is provided to the head space of the storage tank.

4. The system of claim 1 further comprising a gas dispenser in communication with the bank of cascaded storage cylinders.

5. The system of claim 4 wherein the vaporizer also selectively communicates with the gas dispenser so that gas may be dispensed directly from the vaporizer.

6. The system of claim 4 further comprising an odorizer in circuit between the vaporizer and the gas dispenser.

7. The system of claim 1 further comprising an odorizer in circuit between the vaporizer and the storage cylinder.

8. The system of claim 1 further comprising a controller and a liquid level gage in communication with the storage tank, said controller communicating with the pump and the liquid level gage so that the pump is activated and the storage tank is automatically refilled when the liquid therein drops to a predetermined level.

9. The system of claim 8 further comprising a pressure sensor in communication with the pressurizing cylinder and a valve that directs liquid from the pump to the vaporizer and alternatively to the storage tank, said controller in communication with the pressure sensor and the valve so that the pressurizing cylinder is automatically recharged with gas from the vaporizer with the pressure therein drops to a predetermined level.

10. The system of claim 1 further comprising a controller and a pressure sensor in communication with the storage cylinder, said controller communicating with the pump and the pressure sensor so that the pump is activated and the storage cylinder is automatically recharged with gas when the pressure therein drops to a predetermined level.

11. The system of claim 1 wherein the pump is a double-acting, reciprocating pump.

12. The system of claim 1 wherein the pump is positioned within the bulk tank so as to be at least partially submerged in the cryogenic liquid therein.

13. The system of claim 1 further comprising a sump in communication with the bulk tank so as to receive cryogenic liquid therefrom and wherein the pump is positioned in the sump so as to be at least partially submerged in cryogenic liquid.

14. A method of dispensing a cryogenic gas and a cryogenic liquid comprising the steps of:

a) providing a supply of liquid in a bulk tank;

b) providing a liquid storage tank, a pressurizing cylinder and a gas storage cylinder;

c) transferring the liquid to the liquid storage tank;

d) vaporizing liquid from the bulk tank so as to produce a gas;

e) transferring a portion of the gas to the gas storage cylinder and another portion of the gas to the pressurizing cylinder;

f) transferring another portion of the gas to the liquid storage tank to condition the liquid therein;

g) dispensing conditioned liquid from the liquid storage tank using gas from the pressurizing cylinder to pressurize the liquid storage tank; and

h) simultaneously dispensing gas from the gas storage cylinder.

15. The method of claim 14 further comprising the step of adding odorant to the gas prior to step e).

16. The method of claim 14 further comprising the step of dispensing gas from the vaporizer directly.

17. The method of claim 14 further comprising the steps of monitoring a liquid level in the liquid storage tank and a pressure level in the gas storage cylinder and refilling and recharging each, respectively, when the levels therein drop below predetermined levels.

18. A system for dispensing cryogenic fluids comprising:

a) a bulk tank containing a supply of cryogenic liquid;

b) a pump in communication with the bulk tank;

c) a vaporizer selectively in communication with the pump, said vaporizer receiving cryogenic liquid from the bulk tank via the pump so that a cryogenic gas is produced;

d) a CNG module including a bank of cascaded storage cylinders selectively in communication with the vaporizer so as to receive gas therefrom for later dispensing; and

e) an LNG module separate and distinct from the CNG module including;

i. a storage tank selectively in communication with the bulk tank so as to receive cryogenic liquid therefrom and selectively in direct communication with the vaporizer to receive cryogenic gas therefrom to condition the cryogenic liquid in the storage tank;

ii. a pressurizing cylinder selectively in communication with the vaporizer so as to receive cryogenic gas therefrom, said pressurizing cylinder pressurizing said storage tank with gas so that the liquid in the storage tank may be dispensed therefrom as gas is simultaneously dispensed from the bank of cascaded storage cylinders.