# US 10,865,943 B2 · Multi-vessel fluid storage and delivery system > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 10,865,943 B2 - Document ID: US10865943B2 - Status: Granted - Kind: B2 - Application number: 15/739,138 - Filed: 2016-06-29 - Published: 2018-11-01 - Granted: 2020-12-15 - Earliest claimed: 2015-06-29 - Assignees: Westport Power Inc. - Applicants: Westport Power Inc. - Inventors: Gage D. Garner; Melih Ogmen - Web page: https://patentgrep.com/patent/US10865943B2 ## CPC - F17C 7/04: with change of state, e.g. vaporisation - F04B 23/02: having reservoirs - F04B 49/08: Regulating by delivery pressure - F17C 13/02: Special adaptations of indicating, measuring, or monitoring equipment (measuring in general G01) - F17C 13/021: {having the height as the parameter} - F17C 13/025: {having the pressure as the parameter} - F04B 2205/05: Pressure after the pump outlet - F17C 2201/056: Small (<1 m3) - F17C 2201/058: portable (<30 l) - F17C 2205/0146: with details of the manifold - F17C 2205/0335: Check-valves or non-return valves - F17C 2205/0338: Pressure regulators - F17C 2221/033: Methane, e.g. natural gas, CNG, LNG, GNL, GNC, PLNG - F17C 2223/0161: cryogenic, e.g. LNG, GNL, PLNG - F17C 2223/033: Small pressure, e.g. for liquefied gas - F17C 2223/041: Stratification - F17C 2225/0115: dense or supercritical, i.e. at high pressure and high density - F17C 2225/0123: gaseous, e.g. CNG, GNC - F17C 2225/0153: Liquefied gas, e.g. LPG, GPL - F17C 2225/033: Small pressure, e.g. for liquefied gas - F17C 2227/0107: by pressurising the ullage - F17C 2227/0135: Pumps - F17C 2227/0178: in the vessel - F17C 2227/0185: comprising several pumps or compressors - F17C 2227/0309: using another fluid - F17C 2227/0323: in a closed loop - F17C 2227/0393: using a vaporiser - F17C 2227/043: by pressure cascade - F17C 2227/046: by even emptying or filling - F17C 2250/032: using computers - F17C 2250/0408: Level of content in the vessel - F17C 2250/043: Pressure - F17C 2250/0439: Temperature - F17C 2250/0626: Pressure - F17C 2250/0636: Flow or movement of content - F17C 2265/066: for feeding engines for propulsion - F17C 2270/0105: Ships - F17C 2270/0139: Fuel stations - F17C 2270/0168: by vehicles - F17C 2270/0171: Trucks - F17C 2270/0173: Railways - F17C 2270/0176: Buses - F17C 2270/0178: Cars - Y02T 10/30: Use of alternative fuels, e.g. biofuels - 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) - F04B: POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS (machines for liquids, or pumps, of rotary-piston or oscillating-piston type F04C; non-positive-displacement pumps F04D; pumping of fluid by direct contact of another fluid or by using inertia of fluid to be pumped F04F) - Y02T: CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION ## Abstract A multi-vessel fluid storage and delivery system is disclosed which is particularly useful in systems having internal combustion engines which use gaseous fuels. The system can deliver gaseous fluids at higher flow rates than that which can be reliably achieved by vapor pressure building circuits alone, and that keeps pressure inside the storage vessel lower so that it reduces fueling time and allows for quick starts thereafter. The system is designed to store gaseous fluid in liquefied form in a plurality of storage vessels including a primary storage vessel fluidly connected to a pump apparatus and one or more server vessels which together with a control system efficiently stores a liquefied gaseous fluid and quickly delivers the fluid as a gas to an end user even when high flow rates are required. The system controls operation of the pump apparatus as a function of the measured fluid pressure, and controls the fluid pressure in a supply line according to predetermined pressure values based upon predetermined system operating conditions. ## Claims ### Claim 1 A multi-vessel fluid storage and delivery system comprising: a primary storage vessel for storing a gaseous fluid in liquefied and vapor form; said gaseous fluid being in gaseous form at standard temperature and pressure, but stored in liquefied and vapor form in said primary storage vessel; a server storage vessel for storing the gaseous fluid in liquefied and vapor form; a pump apparatus in fluid communication with the primary storage vessel for receiving and pressurizing the fluid therefrom and delivering the fluid to the server storage vessel through a discharge line; a supply line in fluid communication with the server storage vessel for receiving the fluid therefrom and delivering the fluid to an end user; a first vaporizer operable to heat the fluid that flows from the primary storage vessel through the discharge line to transform the fluid into a gaseous state before flowing through a continuation of the discharge line that leads to the server storage vessel; a second vaporizer operable to heat the fluid that flows through the supply line; a pressure sensor for measuring fluid pressure in the discharge line or the supply line; and a control system in communication with: the pressure sensor, to receive fluid pressure measurements from the pressure sensor; and the pump apparatus, to send command signals to the pump apparatus to control operation as a function of the measured fluid pressure to control fluid pressure in the supply line according to predetermined pressure values based upon predetermined operating conditions. ### Claim 2 (depends on 1) The multi-vessel fluid storage and delivery system of claim 1, wherein the predetermined operating conditions include at least one of an end user fluid flow demand, storage vessel liquefied gaseous fluid level, and a measured temperature that correlates to an operational temperature of the first vaporizer. ### Claim 3 (depends on 1) The multi-vessel fluid storage and delivery system of claim 1, further comprising a second pressure sensor associated with a primary vessel vapor line fluidly connecting a vapor space of the primary storage vessel with an inlet into said first vaporizer. ### Claim 4 (depends on 1) The multi-vessel fluid storage and delivery system of claim 1, further comprising: a server vessel vapor line associated with an inlet of the server storage vessel which fluidly connects server storage vessel vapor space with an inlet of the second vaporizer; a bypass vapor line valve disposed in the server vessel vapor line to control flow therethrough; wherein the control system manages flow through the server vessel vapor line as a function of the pressure measurements received from the pressure sensor and predetermined operating conditions that dictate when to withdraw vapor instead of liquefied gaseous fluid from the server storage vessel. ### Claim 5 (depends on 4) The multi-vessel fluid storage and delivery system of claim 4, wherein when the server storage vessel bypass vapor line valve is opened, fluid from the primary storage vessel is directed to the end user therethrough. ### Claim 6 (depends on 4) The multi-vessel fluid storage and delivery system of claim 4, wherein when the server storage vessel bypass vapor line valve is closed, fluid from the primary storage vessel is directed to the server vessel vapor space and liquefied gaseous fluid is thereby directed from the server vessel to said second vaporizer. ### Claim 7 (depends on 4) The multi-vessel fluid storage and delivery system of any one of claim 4, wherein one of the predetermined operating conditions for opening the bypass vapor line valve is when the control system determines the level of liquefied gaseous fluid remaining in the server storage vessel associated with the bypass vapor line valve is below a predetermined level. ### Claim 8 (depends on 4) The multi-vessel fluid storage and delivery system of claim 4, wherein one of the predetermined operating conditions for closing the bypass vapor line valve is when the control system determines the level of liquefied gaseous fluid remaining in the server storage vessel associated with the bypass vapor line valve is higher than a predetermined high vessel level target. ### Claim 9 (depends on 1) The multi-vessel fluid storage and delivery system of claim 1, further comprising a gaseous fluid pressure regulator disposed on the supply line upstream of the end user. ### Claim 10 (depends on 1) The multi-vessel fluid storage and delivery system of claim 1, further comprising a plurality of server storage vessels, each fluidly connected to said primary storage vessel through said discharge line. ### Claim 11 (depends on 10) The multi-vessel fluid storage and delivery system of claim 10, wherein vapor space of each of said plurality of server storage vessels is associated with a pressure sensor for measuring the vapor pressure therein. ### Claim 12 (depends on 10) The multi-vessel fluid storage and delivery system of claim 10, wherein each of said plurality of server storage vessels is associated with an individual server vessel vapor line and a bypass vapor line valve to control flow therethrough. ### Claim 13 (depends on 1) The multi-vessel fluid storage and delivery system of claim 1, wherein the first and second vaporizers are heat exchangers and engine coolant is circulated from an engine coolant system to flow through the respective heat exchangers to transfer heat energy to the gaseous fluid delivered from the respective primary and server storage vessels. ### Claim 14 (depends on 1) The multi-vessel fluid storage and delivery system of claim 1, wherein the pressure sensor measures pressure in the discharge line. ### Claim 15 (depends on 1) The multi-vessel fluid storage and delivery system of claim 1, wherein the pressure sensor measures pressure in the supply line. ### Claim 16 (depends on 1) The multi-vessel fluid storage and delivery system of claim 1, wherein the predetermined pressure values are set based on the end user fluid flow demand. ### Claim 17 (depends on 1) The multi-vessel fluid storage and delivery system of claim 1, wherein the control system commands the pump apparatus to supply fluid to the discharge line when the pressure in at least one of the discharge line and the supply line is below a predetermined low pressure value. ### Claim 18 (depends on 1) The multi-vessel fluid storage and delivery system of claim 1, wherein the control system commands the pump apparatus to stop supply of fluid to the discharge line when the pressure in at least one of the discharge line and the supply line is above a predetermined high pressure value. ### Claim 19 (depends on 1) The multi-vessel fluid storage and delivery system of claim 1, wherein the pressure sensor is part of a dual pressure and temperature sensor, wherein the control system commands the pump apparatus to supply fluid to the discharge line when the pressure in either the discharge line or the supply line is below a predetermined low pressure value and when a measured temperature is above a predetermined high temperature value. ### Claim 20 (depends on 8) The multi-vessel fluid storage and delivery system of claim 8, wherein the predetermined high vessel level target is set as a function of a second highest storage vessel liquefied gaseous fluid level. ### Claim 21 (depends on 1) The multi-vessel fluid storage and delivery system of claim 1, wherein the server storage vessel functions as an accumulator. ### Claim 22 (depends on 1) The multi-vessel fluid storage and delivery system of claim 1, wherein the end user is an internal combustion engine. ### Claim 23 (depends on 1) The multi-vessel fluid storage and delivery system of claim 1, wherein the gaseous fluid is a gaseous fuel selected from one of natural gas, methane, butane, propane, ethane, hydrogen, biogas, or any combination thereof.