Abstract: A reactor includes a shell enveloping a reaction zone, a heat transfer zone, and an isolation zone. The shell is provided with a feed fluid inlet, a product fluid outlet, and an isolation fluid inlet. The reaction zone provides fluid communication between feed fluid inlet and product fluid outlet, and extends though the heat transfer zone and the isolation zone. The isolation zone is located between the heat transfer zone and the product fluid outlet, where a feed fluid, as it flows from the feed fluid inlet and through the reaction zone, is heated by a heat transfer fluid flowing through the heat transfer zone and reacts to form a product fluid that flows out of the shell through the product fluid outlet. A purge fluid in the isolation zone is at a positive pressure relative to a pressure of the heat transfer fluid flowing through the heat transfer zone.

Abstract: An LNG production plant and a method of constructing the LNG production plant is disclosed. The LNG production plant includes at least one plant module and a support structure to support the plant module. Each plant module is dry transported by a heavy lift vessel and subsequently transferred to the support structure without lifting the plant module from a deck of the vessel. The support structure includes a landing substructure onto which the plant module is transferred from the vessel. Landing substructure may be onshore or offshore. The support structure may also include one or more onshore support substructures and a transfer path enabling a plant module to be moved from the landing substructure to a corresponding onshore support substructure.

Abstract: An LNG production plant positioned at a production location adjacent to a body of water is described. The LNG production plant includes a plurality of spaced-apart facilities including a first facility and a second facility, each facility provided with plant equipment related to a pre-determined function associated with the production of LNG, where the first facility is an onshore facility and the second facility is an integrated storage/offloading facility arranged on a gravity-based structure having a base that rests on the seabed at a selected location within the body of water.

Abstract: An LNG production plant and a method of constructing the LNG production plant is disclosed. The LNG production plant includes at least one plant module and a support structure to support the plant module. Each plant module is dry transported by a heavy lift vessel and subsequently transferred to the support structure without lifting the plant module from a deck of the vessel. The support structure includes a landing substructure onto which the plant module is transferred from the vessel. Landing substructure may be onshore or offshore. The support structure may also include one or more onshore support substructures and a transfer path enabling a plant module to be moved from the landing substructure to a corresponding onshore support substructure.

Abstract: An LNG processing plant positioned at a processing location adjacent to a body of water is described. The LNG processing plant includes A) a first phase LNG processing plant for processing an initial plant capacity of LNG, the first phase LNG processing plant including a plurality of first phase facilities, each first phase facility provided with plant equipment related to a pre-determined function associated with the processing of LNG, wherein one or more of the plurality of first phase facilities is arranged on a deck of a structure wherein the deck is arranged above the level of the water at a selected offshore or near-shore location; and, B) one or more second phase facilities provided on the deck of the structure to provide a second phase LNG processing plant, said second phase LNG processing plant having a maximum plant capacity that is higher than the initial plant capacity.

Abstract: An LNG production plant positioned at a production location adjacent to a body of water is described. The LNG production plant includes a plurality of spaced-apart facilities including a first facility and a second facility, each facility provided with plant equipment related to a pre-determined function associated with the production of LNG, where the first facility is an onshore facility and the second facility is an integrated storage/offloading facility arranged on a gravity-based structure having a base that rests on the seabed at a selected location within the body of water.

Abstract: A process and apparatus for regasification of LNG to form natural gas using ambient air as the primary source of heat are described. LNG is directed to flow through an ambient air vaporizer to form a natural gas stream through direct heat exchange between the LNG and ambient air. The temperature of the natural gas stream is adjusted to suit a predetermined delivery temperature in a trim heater exchanging heat with a circulating intermediate fluid. The intermediate fluid is directed to flow through an ambient air heater such that the intermediate fluid exchanges heat with ambient air. Heat transfer between the ambient air and the LNG is assisted using one or more force draft fans to direct the flow of ambient air over the ambient air heater and the ambient air vaporizer in turn to dry the ambient air before it arrives at the ambient air vaporizer.

Abstract: Liquefied natural gas is regasified to form natural gas, including circulation of an intermediate fluid between a vaporizer and an ambient air heater, where the intermediate fluid is warmed by exchanging heat with the ambient air as the intermediate fluid passes through the ambient air heater, and the intermediate fluid is cooled by exchanging heat with LNG as the intermediate fluid passes through the vaporizer. The ambient air heater is subjected to a defrosting cycle by intermittently regulating the temperature of the intermediate fluid fed to the ambient air heater to a temperature greater than zero degrees Celsius using a source of supplemental heat.

Abstract: A process and corresponding apparatus for regasifying a cryogenic liquid to gaseous form includes a process step and suitable structure to transfer heat from ambient air to the cryogenic liquid across a heat transfer surface by circulating the cryogenic liquid or an intermediate fluid through an atmospheric vaporizer, where the ambient air and the cryogenic fluid or intermediate fluid are not in direct contact; and a process step and suitable structure to mechanically scrape an external portion of the heat transfer surface exposed to the atmosphere to remove frost from the external portion of the heat transfer surface, where defrosting is achieved without the need to discontinue circulating the cryogenic fluid or the intermediate fluid through the atmospheric vaporizer.

Abstract: The present invention relates to a process and system for managing boil-off gas generated during ship-to-ship transfer of LNG at sea. The LNG is transferred from a storage tank onboard a delivery vessel to a storage tank onboard a receiving vessel. The process includes the steps of a) operating the receiving vessel storage tank at a pressure greater than the operating pressure of the delivery vessel storage tank; and, b) transferring a portion of the boil-off gas from the receiving vessel storage tank to the delivery vessel storage tank onboard.

Abstract: The present invention relates to a power generation system for a marine vessel including a gas-fired power generation unit such as a gas turbine arranged to receive unodorized natural gas that has been vaporized from LNG stored onboard the marine vessel as a source of fuel gas. Unodorized natural gas is used a source of fuel to keep air emissions to a minimum.

Abstract: The present invention relates to a process and apparatus for regasifying a cryogenic liquid to gaseous form. Heat is transferred from ambient air to the cryogenic liquid across a heat transfer surface by circulating the cryogenic liquid or an intermediate fluid through an atmospheric vaporizer, wherein he ambient air and the cryogenic fluid or intermediate fluid are not in direct contact. A layer of ice forms on an external portion of the heat transfer surface exposed to the atmosphere where the temperature at the heat transfer surface is below the freezing temperature of water. The layer of ice is dislodged intermittently from the vaporizer using a source of heat operatively associated with a control device, the control device arranged to generate a signal when de-icing is required. De-icing is achieved without the need to discontinue circulating the cryogenic fluid or the intermediate fluid through the vaporizer.

Abstract: A method is provided for offshore regasification of liquid natural gas (LNG) for delivery onshore as a gas. The method includes offloading LNG from a first LNG Carrier to a second LNG Carrier at an offloading location, the second LNG Carrier including an onboard regasification facility, transferring the second LNG Carrier from the offloading location to a mooring location closer to shore, regasifying the LNG onboard the second LNG Carrier to form natural gas, and transferring the regasified natural gas to an onshore gas distribution facility for delivery to an end user.

Abstract: Liquefied natural gas is regasified to form natural gas, including circulation of an intermediate fluid between a vaporizer and an ambient air heater, where the intermediate fluid is warmed by exchanging heat with the ambient air as the intermediate fluid passes through the ambient air heater, and the intermediate fluid is cooled by exchanging heat with LNG as the intermediate fluid passes through the vaporizer. The ambient air heater is subjected to a defrosting cycle by intermittently regulating the temperature of the intermediate fluid fed to the ambient air heater to a temperature greater than zero degrees Celsius using a source of supplemental heat.

Abstract: Offshore regasification of liquid natural gas (LNG) is provided onboard an LNG carrier vessel for delivery onshore as a gas. The LNG is regasified to natural gas aboard the LNG carrier vessel using ambient air as the primary source of heat for regasification. Condensed water that accumulates from the ambient air during the regasification of LNG is collected, and the collected condensed water is used as ballast for the LNG carrier vessel.

Abstract: A process and apparatus for regasification of LNG to form natural gas using ambient air as the primary source of heat are described. LNG is directed to flow through an ambient air vaporizer to form a natural gas stream through direct heat exchange between the LNG and ambient air. The temperature of the natural gas stream is adjusted to suit a predetermined delivery temperature in a trim heater exchanging heat with a circulating intermediate fluid. The intermediate fluid is directed to flow through an ambient air heater such that the intermediate fluid exchanges heat with ambient air. Heat transfer between the ambient air and the LNG is assisted using one or more force draft fans to direct the flow of ambient air over the ambient air heater and the ambient air vaporizer in turn to dry the ambient air before it arrives at the ambient air vaporizer.