Chevron U.s.a. Inc.

John S Hartono

Kenneth W Sheets, Jr

Jimmie Dean Adkins

Paul Martella

Donald Gregory Danmeier

A liquefied natural gas (LNG) transport vessel for transporting liquefied natural gas (LNG) is disclosed which is capable of storing excess boil off gas BOG until needed for combustion in one or more combustion apparatus on the vessel. A method for managing the delivery of the BOG to the combustion apparatus is also described. The LNG vessel includes at least one insulated LNG storage tank which stores LNG. A first stage LNG receiver receives and stores BOG from the at least one LNG storage tank. A second stage or high pressure BOG storage tank receives compressed BOG from the receiver and stores the BOG as needed for combustion by one or more combustion apparatus of the vessel. A pressure regulator allows BOG gas to be delivered to the combustion apparatus if there is sufficient pressure in the high pressure storage tank to passively deliver the BOG at a predetermined delivery pressure. If the pressure in the high pressure BOG storage tank is insufficient to passively delivery the BOG to combustion apparatus, then a combustion apparatus compressor may be used to actively increase the pressure in BOG such that the BOG is delivered at the necessary delivery pressure. If there is still insufficient BOG in the high pressure BOG storage tank, then it may be necessary to supply supplemental auxiliary fuel to meet the needs of the combustion apparatus.

LNG transport vessel and method for storing and managing excess boil off gas thereon

A process and apparatus are provided for transferring fluids such as, for example, liquefied natural gas between a source structure such as a floating storage vessel and a receiving structure such as a floating transport vessel utilizing a controllable deployment system to deploy a fluid conduit. The fluid conduit end is supported by a mooring device which is positioned by the controllable deployment system. A transfer vessel is also provided which utilizes the controllable deployment system to position and support a fluid conduit for connection with a manifold on a receiving vessel. The deployment system operates in active mode during positioning and in passive mode during fluid transfer. The fluid transfer system disclosed allows safe, controlled operation and fluid transfer in open sea conditions.

Process, apparatus and vessel for transferring fluids between two structures

An apparatus for transferring a cryogenic fluid. The apparatus includes a conduit having an inlet and an outlet, a source of cryogenic fluid connected to the inlet for providing cryogenic fluid to the conduit and a cool down line connected to the conduit at an intermediate port between the inlet and the outlet, the cool down line in fluid communication with the source of cryogenic fluid for providing cryogenic fluid to the conduit through the intermediate port. The cool down line can be external and intersect with the conduit at the intermediate port, or may be disposed within the conduit. The conduit may have more than one intermediate port for providing cryogenic fluid to the conduit downstream from the inlet. Such an apparatus enables a conduit for transferring a cryogenic fluid to be pre-cooled to a cryogenic temperature more quickly so that transfer operations can begin.

Apparatus for transferring a cryogenic fluid

A method for loading LNG on a floating vessel through a conduit having the inlet, an outlet and an intermediate port located between the inlet and the outlet. The method includes the step of pumping a reduced flow of LNG into the inlet and the step of pumping a reduced flow of LNG into the intermediate port so that different sections of the conduit can be cooled simultaneously. When the conduit has cooled to a temperature suitable for transferring LNG, the method further includes pumping an increased flow of the LNG into the inlet of the conduit. The LNG can then be directed from the outlet to a storage tank onboard a floating vessel.

Method for loading LNG on a floating vessel

A method for transferring a cryogenic fluid from a floating vessel. The cryogenic fluids to be transferred can include liquefied hydrocarbon gases such as LNG. The method includes the steps of pumping a reduced flow of a cryogenic fluid into a first end and/or a second end of a conduit to begin pre-cooling the conduit. Pre-cooling also includes pumping a reduced flow of the cryogenic fluid into the conduit at a point intermediate the first end and the second end so that different sections of the conduit are cooled simultaneously. When the conduit has cooled to a temperature suitable for transferring the cryogenic fluid, an increased flow of the cryogenic fluid is pumped into the first end of the conduit to transfer the cryogenic fluid from the floating vessel. The cryogenic fluid can then be directed from the second end of the conduit to a storage tank on shore or onboard a second floating vessel.

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Alameda, CA, United States of America

John S Hartono