Compressed and liquified natural gas storage and dispensing system
10539271 ยท 2020-01-21
Assignee
Inventors
Cpc classification
F17C13/084
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F17C2225/0123
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F17C7/04
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F17C2223/0123
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F17C2223/036
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F17C2265/065
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F17C2225/036
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F17C2260/025
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F17C2265/032
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F17C2250/01
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F17C2223/0161
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F17C5/02
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F17C2227/0135
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F17C2227/03
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F17C2205/013
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F17C5/06
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F17D1/04
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F17C2221/033
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
International classification
F17C5/06
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F17D1/04
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
Abstract
A compressed natural gas storage and dispensing system having bulk storage tanks in fluid communication with a natural gas supply source; a compressor to produce compressed natural gas; dispensing storage tanks in fluid communication with the bulk storage tanks and in fluid communication with fuel dispensers; a liquified natural gas storage tank in fluid communication with the bulk storage tanks, wherein compressed natural gas resulting from vaporization of the liquified natural gas within the liquified natural gas storage tank is transferred to the bulk storage tanks as a supplemental source of compressed natural gas, or wherein liquified natural gas is vaporized in an ambient vaporizer and delivered to the bulk or dispensing storage tanks.
Claims
1. A compressed natural gas storage and dispensing system comprising: a CNG bulk storage bank in fluid communication with a natural gas supply source and in fluid communication with CNG fuel dispensers; a LNG storage tank in fluid communication with said CNG bulk storage bank, whereby CNG vaporized from LNG retained within said LNG storage tank is delivered to said CNG bulk storage bank; a pump in fluid communication with said LNG storage tank, and a vaporizer in fluid communication with said pump and with said CNG bulk storage bank, whereby LNG is pumped from said LNG storage tank to said vaporizer for conversion to CNG and delivery to said CNG bulk storage bank; LNG fuel dispensers in fluid communication with said pump, whereby LNG is pumped from said LNG storage tank to said LNG fuel dispensers; a heat exchanger in fluid communication with said vaporizer and said CNG bulk storage bank; and a CNG dispensing storage bank disposed in fluid communication between said CNG bulk storage bank and said CNG fuel dispensers, wherein said vaporizer is also in fluid communication with said CNG dispensing storage bank, whereby CNG from said vaporizer may also be delivered to said CNG dispensing storage bank without passing through said CNG bulk storage bank.
2. The system of claim 1, wherein said CNG bulk storage bank comprises bulk storage tanks in fluid communication with said natural gas supply source; and wherein said CNG dispensing storage bank comprises dispensing storage tanks; said system further comprising: a primary compressor drawing natural gas from said supply source, compressing the natural gas to a desired pressure, and delivering the natural gas to said bulk storage tanks; a secondary compressor receiving said natural gas from said bulk storage tanks, recompressing the natural gas to a desired pressure, and delivering said natural gas to said dispensing storage tanks; wherein when the pressure within said dispensing storage tanks falls below a first designated minimum pressure, natural gas is delivered from said bulk storage tanks to said dispensing storage tanks, and wherein when the pressure in said bulk storage tanks falls below a second designated minimum pressure, natural gas is delivered from said supply source to said bulk storage tanks.
3. The system of claim 2, further comprising a pump in fluid communication with said LNG storage tank, and a vaporizer in fluid communication with said pump and with said bulk storage tanks, whereby LNG is pumped from said LNG storage tank to said vaporizer for conversion to CNG and delivery to said bulk storage tanks.
4. The system of claim 3, further comprising a heat exchanger in fluid communication with said vaporizer and said bulk storage tanks.
5. The system of claim 3, wherein said vaporizer is also in fluid communication with said dispensing storage tanks, whereby CNG from said vaporizer may also be delivered to said dispensing storage tanks.
6. The system of claim 3, further comprising LNG fuel dispensers in fluid communication with said pump, whereby LNG is pumped from said LNG storage tank to said LNG fuel dispensers.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
(1)
(2)
DETAILED DESCRIPTION
(3) With reference to the drawings, embodiments of the invention will now be described in enabling detail. The invention is a compressed natural gas (CNG) fuel island system and method of dispensing CNG to individual CNG adapted vehicles on demand. The term fuel island is used herein to refer to a facility in the nature of a gas station, wherein the fuel island broadly comprises receiving, storage and dispensing apparatuses for CNG. In the invention as presented herein, the fuel island further comprises receiving, storing and dispensing apparatuses for liquified natural gas (LNG), wherein vaporized natural gas from the LNG storage apparatuses are delivered to the CNG storage apparatuses, such that the LNG is available as a supplement to the CNG when needed.
(4) A first embodiment of the system and method is shown in
(5) The CNG receiving, storing and dispensing fast-fill fuel island system 10 further comprises a LNG receiving, storing and dispensing supplemental system 70. The system comprises at least one LNG storage tank 71 that receives and maintains LNG delivered from off-site. As vaporization, also known as boil-off, of the LNG occurs within LNG stage tank 71, CNG is formed. This LNG and vaporization CNG is utilized as a supplemental source of CNG for the fuel island system 10 in addition to the CNG received through the CNG pipeline 90 or equivalent means. Both the supplemental CNG and the LNG is available to address potential problems resulting from excessive vehicle demand, shortages or inconsistent natural gas delivery from off-site, or drops in pressure within the CNG banks 20 or 30.
(6) The LNG system 70 is structured such that this supplemental CNG may be distributed from the LNG tank 71 through supplemental conduits 92 directly to the CNG storage bank 30 in order to refill or raise the pressure in the CNG storage bank 30. In a second scenario, the LNG is extracted from the LNG tank 71 by a cryogenic pump 72 and delivered to an ambient vaporizer 73 for conversion to CNG. Optionally, this converted CNG or additional LNG may then be processed through a heat exchanger 75 to produce a greater amount of CNG. After being treated in an odorizer 74, the CNG is then delivered to CNG storage bank 30 or CNG dispensing bank 20 to refill or raise the pressure within the banks 30/20. In still another embodiment, LNG from the LNG storage tank 71 may be delivered directly to LNG fuel dispensers 76 for the refueling of LNG adapted vehicles.
(7) An alternative embodiment of the method and system is shown in
(8) The storage tank banks 20 and 30 are connected together with manifold pipelines 40 and appropriate valves 41. Preferably the tanks 21/31 are resin composite tanks of the type known in the industry as type 4, 4/5 or 5, as tanks of this composition are capable of holding more gas at high pressure and at lower cost of manufacture than conventional metal tanks. The number of tanks 21/31 is dependent on how much fuel will need to be stored and how much fuel should be available for dispensing at a particular site dependent on demand. A sufficient number of dispensing storage tanks 21 should be provided to meet the projected peak fueling requirements of the fuel island system 10, to be measured in standard cubic feet per minute (scfm). The number of bulk storage tanks 31 is determined as a result of the expected demand on the dispensing storage tanks 21, but there will be a significantly greater number of bulk storage tanks 31 than dispensing storage tanks 21. The bulk storage tanks 31 are filled in sequence through the action of primary compressors 51 that compress the natural gas delivered at low pressure from the pipeline 90 or other source up to a desired high pressure (5000 psi for example), and are filled whenever the pressure within a bulk storage tank 31 falls below a predetermined pressure, regardless of whether or not fuel is being dispensed through a dispensing storage tank 21. Because of the large number of bulk storage tanks 31, the refilling process can be at a relatively low flow rate, since the supply of natural gas is continuous and draw down on the bulk storage tanks 31 occurs only during refilling of the dispensing storage tanks 21 whenever pressures in the dispensing storage tanks 21 are reduced to predetermined minimum levels (3600 psi for example).
(9) Compressors 51/52 draw the gas through the system 10 via suction, the compressors 51/52 being activated by sensors when pressure in either the bulk storage tanks 31 or the dispensing storage tanks 21 is reduced to a predetermined level. The valves 41 that transfer the gas to and from tanks 21/31 and compressors 51/52 operate automatically based on pressures, timers and temperatures, with the valves 41 being monitored by a sequencing panel. The sequencing panel will also have the ability to allow manual override of the valves 41. The goal of the storage system 10 is to insure the dispensing storage tanks 21 are filled to maximum fuel capacity at all times. The storage system 10 will also have safety monitoring for fire, smoke, heat, and UV hydrocarbon detection with overhead fire protection deployment such as sprinkler systems loaded with fire suppressants.
(10) The CNG receiving, storing and dispensing fast-fill fuel island system 10 of this
(11) The LNG system 70 is structured such that this supplemental CNG may be distributed from the LNG tank 71 through supplemental conduits 92 directly to the CNG storage tanks 31 in order to refill or raise the pressure in the CNG storage tanks 31. In a second scenario, the LNG is extracted from the LNG tank 71 by a cryogenic pump 72 and delivered to an ambient vaporizer 73 for conversion to CNG. Optionally, this converted CNG or additional LNG may then be processed through a heat exchanger 75 to produce a greater amount of CNG. After being treated in an odorizer 74, the CNG is then delivered to CNG storage tanks 31 or CNG dispensing tanks 21 to refill or raise the pressure within the tanks 31/21. In still another embodiment, LNG from the LNG storage tank 71 may be delivered directly to LNG fuel dispensers 76 for the refueling of LNG adapted vehicles.
(12) A major advantage of the system as described is its ability to provide to the CNG dispensers 60 a sufficient quantity of CNG at the desired minimum pressure for efficient delivery to the motor vehicles, wherein the source of the natural gas is a low pressure, low flow rate and fluctuating volume source, by utilizing relatively low horsepower compressors 51/52. For example, 50-150 horsepower compressors 51/52 may be utilized. Conventionally such low horsepower compressors would not be able to provide CNG above a minimum desired psi at a flow rate suitable for refilling vehicles in a timely manner, and therefore known systems utilize compressors of much greater horsepower, which are incrementally more expensive. Because the filling of the bulk storage tanks 31 does not need to be rapid and instead may be accomplished over long time periods, and because the CNG delivered from the bulk storage tanks 31 is passed through secondary compressors to recompress the CNG prior to delivery to the dispensing storage tanks 21, these 50-150 horsepower compressors are sufficient. In addition, the utilization of LNG stored on site and the CNG produced by vaporization of the LNG provides supplemental CNG when needed.
PROPHETIC EXAMPLE
(13) As shown in
(14) Bank 20 provides fuel to the fuel dispensers 60 on an on-demand basis. When the pressure within the dispensing storage tanks 21 falls below 3600 psi, valves 41 open to draw gas from bank 30 into bank 20, the gas drawn from tanks 31 being recompressed to at least 5,000 psi prior to delivery to bank 20. Preferably, gas will be drawn from tanks 31 sequentially, such that when pressure in a first bulk storage tank 31 falls below the predetermined minimum pressure, output from the first tank 31 is stopped and gas is taken from a second tank 31, etc., until all dispensing tanks 21 are refilled. When output from the first tank 31 is stopped, or even possibly during the delivery of gas from the first tank 31, primary compressors 51 start refilling of this first bulk storage tank 31 from the natural gas source pipeline 90. This system insures that there will always be a sufficient supply of natural gas at the required pressure (5000 psi) to be used as needed by fuel island demand.
(15) Preferably, the tanks 21/31 in the example are designed to handle at least 5,000 psi, and preferably higher, and should be cylindrical and double stacked; a suitable size being 21 inches in diameter and 84 inches long, so they can fit below grade into the fuel island culvert design of patent application Ser. No. 13/506,898. As previously discussed, type 4, 4/5 or 5 tanks composed of a resin or hybrid are preferred. The same system can be employed above ground, independent of the fuel island culvert design. The higher the psi, the more gas can be stored in the tanks 21/31. Whenever psi falls to 3,600 or below, the tanks 21/31 will automatically refill from their respective source via the compressor units 51/52. In the event that there is an insufficient supply of CNG available for dispensing, the supplemental CNG from the LNG system 70 is utilized as described above.
(16) The system 10 as described comprises features advantageous, novel and non-obvious over the known prior art systems. The system allows for reduced time to fill-up using CNG, similar to conventional fueling with gasoline or diesel; addresses problem of insufficient CNG quantity or pressure by utilizing the LNG supplemental CNG source; greater access to CNG fueling for non-fleet vehicles, as most CNG stations are restricted to fleets due to the time it takes to fill a vehicle and the limited supply of CNG available for compression; which results in most fleet CNG stations scheduling fill-ups by appointment only; uninterrupted, continuous and systematic supply of CNG fuel to dispenser(s); CNG stations will be more attractive to investors and more accepting by the public because CNG will be dispensed faster and efficiently without the fear of spending too much time at a dispenser and without fear of not having enough fuel to fill up at a convenient time and will have lower installation and operational costs.
(17) It is contemplated and understood that equivalents and substitutions for certain elements described above may be obvious to those of ordinary skill in the art, and therefore the true scope and definition of the invention is to be as set forth in the following claims.