# US 5,699,839 A · Zero-vent liquid natural gas fueling station > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 5,699,839 A - Document ID: US5699839A - Status: Granted - Kind: A - Application number: 08/502,678 - Filed: 1995-07-14 - Granted: 1997-12-23 - Earliest claimed: 1995-07-14 - Assignees: Acurex Environmental Corporation - Inventors: Hans-Joachim Dehne - Web page: https://patentgrep.com/patent/US5699839A ## CPC - F17C 9/00: Methods or apparatus for discharging liquefied or solidified gases from vessels not under pressure - F17C 6/00: Methods and apparatus for filling vessels not under pressure with liquefied or solidified gases - F17C 2201/0119: with flat end-piece - F17C 2201/056: Small (<1 m3) - F17C 2203/0391: by vacuum - F17C 2205/0142: bundled in parallel - F17C 2205/0146: with details of the manifold - F17C 2205/0314: breakable, e.g. with burst discs - F17C 2205/0323: Valves - F17C 2205/0326: electrically actuated - F17C 2205/0332: Safety valves or pressure relief valves - F17C 2205/037: Quick connecting means, e.g. couplings - F17C 2221/033: Methane, e.g. natural gas, CNG, LNG, GNL, GNC, PLNG - F17C 2223/0161: cryogenic, e.g. LNG, GNL, PLNG - F17C 2227/0157: Compressors - F17C 2227/0304: using an electric heater - F17C 2260/035: of fluid - F17C 2265/065: for refuelling vehicle fuel tanks - F17C 2270/0139: Fuel stations - F17C 2270/0168: by vehicles - 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 (storing fluids in natural or artificial cavities or chambers in the earth B65G5/00; construction or assembling of bulk storage containers employing civil-engineering techniques E04H7/00; variable-capacity gas-holders F17B; liquefaction or refrigeration machines, plants, or systems F25) ## Abstract A liquefied natural gas (LNG) fueling station which does not vent natural gas vapors. Three cryogenic storage vessels alternately serve as dispensing, conditioning, and receiving vessels. A natural gas compressor transfers vapor between the vessels and evacuates vapors vented from tanker trucks and vehicles. Heat absorbed by the LNG is utilized to warm the fuel for use in vehicles by bubbling the vapors through the LNG in the conditioning vessel. ## Claims ### Claim 1 A method of operating a liquid natural gas fueling station comprising first, second, and third cyrogenic storage vessels, wherein said first vessel contains natural gas vapor and said second and third vessels contain liquid natural gas, comprising: (a) lowering the vapor pressure in said first vessel by extracting natural gas vapor therefrom, which also lowers the temperature of liquid natural gas, if present, in said first vessel; (b) conducting said extracted vapor into at least one of the following: 1) said second vessel to pressurize said second vessel; 2) said liquid in said third vessel; (c) introducing liquid natural gas into said first vessel; (d) dispensing liquid natural gas from said second vessel; and (e) repeating steps (a) through (d) using said second vessel in steps (a) and (c), said first vessel in step (b2), and said third vessel in steps (b1) and (d). ### Claim 2 (depends on 1) The method of claim 1 wherein liquid natural gas is introduced in step (c) into said first vessel by pressure transfer. ### Claim 3 (depends on 2) The method of claim 2 wherein liquid natural gas is dispensed from said second vessel in step (d) by pressure transfer. ### Claim 4 (depends on 3) The method of claim 3 wherein vapor is extracted from said first vessel in step (a) until the pressure of the natural gas vapor in said first vessel is lowered below fifty psig. ### Claim 5 (depends on 4) The method of claim 4 wherein vapor is extracted from said first vessel in step (a) until the pressure of the natural gas vapor in said first vessel is lowered to about fifteen psig. ### Claim 6 (depends on 3) The method of claim 3 wherein said extracted vapor is conducted in step (b) into the top of said second vessel until said second vessel is pressurized to the pressure required to dispense liquid natural gas therefrom in step (d). ### Claim 7 (depends on 6) The method of claim 6 wherein said extracted vapor is conducted in step (b) into the top of said second vessel until said second vessel is pressurized to above one-hundred and seventy-five psig. ### Claim 8 (depends on 6) The method of claim 6 wherein after said second vessel is pressurized to above one-hundred and seventy-five psig, said extracted vapor is conducted to the liquid in said third vessel after completion of fueling from said first vessel. ### Claim 9 (depends on 3) The method of claim 3 further including the step of venting natural gas vapor from the fuel storage tank of a vehicle into the liquid in said third vessel. ### Claim 10 (depends on 3) The method of claim 3 further including the step of venting natural gas vapor from a tanker into at least one of the following: the liquid natural gas in said third vessel, or the liquid natural gas in said second vessel. ### Claim 11 (depends on 10) The method of claim 10 wherein said vapor from said tanker is vented into the liquid in said second vessel after the liquid natural gas in said third vessel has reached a saturation pressure of at least fifty psig. ### Claim 12 A liquid natural gas fueling station for receiving fuel from a tanker and dispensing fuel to a fuel storage tank of a vehicle, comprising: (a) first, second, and third cryogenic storage vessels for holding liquid natural gas; (b) a compressor having an inlet and an outlet; (c) a receiving system including 1) a receiving connection for coupling to the fuel line of said tanker and receiving liquid natural gas from said tanker, and 2) a tanker venting connection for coupling to the vent line of said tanker and receiving natural gas vapor from said tanker; (d) a dispensing system including 1) a dispensing connection for coupling to the fuel line of said vehicle and dispensing liquid natural gas to said vehicle, and 2) a vehicle venting connection for coupling to the vent line of the vehicle and receiving natural gas vapor from said vehicle; and (e) a manifold system connecting 1) a top port of said first vessel to the inlet of said compressor, and the outlet of said compressor to one of a top port of said second vessel and a bottom port of said third vessel when preparing said second vessel to dispense liquid natural gas and said third vessel to receive liquid natural gas, 2) said dispensing connection to a bottom port of said second vessel and said vehicle venting connection to said bottom port of said third vessel when dispensing liquid natural gas to a vehicle, 3) said receiving connection to a top port of said first vessel and said tanker venting connection to one of said bottom port of said first vessel and the inlet of said compressor when receiving liquid natural gas from a tanker, and the outlet of said compressor to a bottom port of said third vessel if said tanker venting connection is connected to the inlet of said compressor. ### Claim 13 (depends on 12) The fueling station of claim 12 further comprising means for using said second vessel in place of said first vessel, said first vessel in place of said third vessel, and said third vessel in place of said second vessel.