EP3980704A1 - Système de liquéfaction de gaz naturel - Google Patents

Système de liquéfaction de gaz naturel

Info

Publication number
EP3980704A1
EP3980704A1 EP20732488.0A EP20732488A EP3980704A1 EP 3980704 A1 EP3980704 A1 EP 3980704A1 EP 20732488 A EP20732488 A EP 20732488A EP 3980704 A1 EP3980704 A1 EP 3980704A1
Authority
EP
European Patent Office
Prior art keywords
energy
electric
refrigerant
power
natural gas
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
EP20732488.0A
Other languages
German (de)
English (en)
Inventor
Paolo NOCCIONI
Oriano ZUCCHI
Andrea ALFANI
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nuovo Pignone Technologie SRL
Original Assignee
Nuovo Pignone Technologie SRL
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nuovo Pignone Technologie SRL filed Critical Nuovo Pignone Technologie SRL
Publication of EP3980704A1 publication Critical patent/EP3980704A1/fr
Pending legal-status Critical Current

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Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/0002—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the fluid to be liquefied
    • F25J1/0022—Hydrocarbons, e.g. natural gas
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/0002—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the fluid to be liquefied
    • F25J1/0012—Primary atmospheric gases, e.g. air
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/003—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production
    • F25J1/0032—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production using the feed stream itself or separated fractions from it, i.e. "internal refrigeration"
    • F25J1/004—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production using the feed stream itself or separated fractions from it, i.e. "internal refrigeration" by flash gas recovery
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/02—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process
    • F25J1/0201—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process using only internal refrigeration means, i.e. without external refrigeration
    • F25J1/0202—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process using only internal refrigeration means, i.e. without external refrigeration in a quasi-closed internal refrigeration loop
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/02—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process
    • F25J1/0228—Coupling of the liquefaction unit to other units or processes, so-called integrated processes
    • F25J1/0229—Integration with a unit for using hydrocarbons, e.g. consuming hydrocarbons as feed stock
    • F25J1/023—Integration with a unit for using hydrocarbons, e.g. consuming hydrocarbons as feed stock for the combustion as fuels, i.e. integration with the fuel gas system
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/02—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process
    • F25J1/0243—Start-up or control of the process; Details of the apparatus used; Details of the refrigerant compression system used
    • F25J1/0244—Operation; Control and regulation; Instrumentation
    • F25J1/0245—Different modes, i.e. 'runs', of operation; Process control
    • F25J1/0251—Intermittent or alternating process, so-called batch process, e.g. "peak-shaving"
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/02—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process
    • F25J1/0243—Start-up or control of the process; Details of the apparatus used; Details of the refrigerant compression system used
    • F25J1/0279—Compression of refrigerant or internal recycle fluid, e.g. kind of compressor, accumulator, suction drum etc.
    • F25J1/0281—Compression of refrigerant or internal recycle fluid, e.g. kind of compressor, accumulator, suction drum etc. characterised by the type of prime driver, e.g. hot gas expander
    • F25J1/0282—Steam turbine as the prime mechanical driver
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/02—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process
    • F25J1/0243—Start-up or control of the process; Details of the apparatus used; Details of the refrigerant compression system used
    • F25J1/0279—Compression of refrigerant or internal recycle fluid, e.g. kind of compressor, accumulator, suction drum etc.
    • F25J1/0281—Compression of refrigerant or internal recycle fluid, e.g. kind of compressor, accumulator, suction drum etc. characterised by the type of prime driver, e.g. hot gas expander
    • F25J1/0283—Gas turbine as the prime mechanical driver
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/02—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process
    • F25J1/0243—Start-up or control of the process; Details of the apparatus used; Details of the refrigerant compression system used
    • F25J1/0279—Compression of refrigerant or internal recycle fluid, e.g. kind of compressor, accumulator, suction drum etc.
    • F25J1/0281—Compression of refrigerant or internal recycle fluid, e.g. kind of compressor, accumulator, suction drum etc. characterised by the type of prime driver, e.g. hot gas expander
    • F25J1/0284—Electrical motor as the prime mechanical driver
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/02—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process
    • F25J1/0243—Start-up or control of the process; Details of the apparatus used; Details of the refrigerant compression system used
    • F25J1/0279—Compression of refrigerant or internal recycle fluid, e.g. kind of compressor, accumulator, suction drum etc.
    • F25J1/0285—Combination of different types of drivers mechanically coupled to the same refrigerant compressor, possibly split on multiple compressor casings
    • F25J1/0287—Combination of different types of drivers mechanically coupled to the same refrigerant compressor, possibly split on multiple compressor casings including an electrical motor
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2210/00—Processes characterised by the type or other details of the feed stream
    • F25J2210/06—Splitting of the feed stream, e.g. for treating or cooling in different ways
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2240/00—Processes or apparatus involving steps for expanding of process streams
    • F25J2240/80—Hot exhaust gas turbine combustion engine
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2260/00—Coupling of processes or apparatus to other units; Integrated schemes
    • F25J2260/30—Integration in an installation using renewable energy

Definitions

  • the present disclosure relates to natural gas liquefaction technology. More specifically, disclosed herein are novel systems and methods for efficiently liquefying a hydrocarbon feed stream, such as a natural gas feed stream.
  • Natural gas is a mixture of hydrocarbons in a gaseous state. Natural gas com prises predominantly methane and can contain a portion of other, heavier gaseous com- ponents. It is useful to liquefy natural gas for a number of reasons and mainly for storage and transportation purposes. Liquefied natural gas (also referred to with the acronym LNG) occupies a much smaller volume and can thus be transported for in stance with LNG vessels. Liquefied natural gas is not only easier to transport because of the smaller volume occupied, but also safer. [0003] Several natural gas liquefaction methods have been developed over the last decades.
  • the natural gas is processed through a plurality of cooling stages using heat exchangers to progressively reduce the temperature of the gas until liquefaction.
  • the refrigeration and liquefaction process is relatively energy consuming.
  • Compressors or compressor trains are required to process cryogenic fluids, i.e. refrig erant fluids, which are used to remove heat from the natural gas stream until liquefac tion.
  • Refrigerant compressors are usually driven by gas turbine engines, steam tur bines or electric motors and they require large quantities of power.
  • a part of the same natural gas which is to be cooled and liquefied is generally used as the main source of energy to run the refrigerant compressors, for instance to generate steam to run a steam turbine, or combustion gas to run a gas turbine engine, which in turn directly drive one or more refrigerant compressors or compressor trains, or else are used to drive electric generators.
  • the electric energy thus generated is used to power electric motors, which drive the refrigerant compressors or compressor trains.
  • Using electric generators to produce electric energy from mechanical energy and electric motors to convert electric energy into mechanical energy to drive the refrigerant compressors avoids the need to run steam or gas turbines at variable speed to adapt the rotational speed to variable flowrate requests from the refrigerant compressors.
  • the driver of the electric generator can rotate at constant speed thus maximizing the efficiency of the driver, while a var iable speed electric motor can in turn drive the refrigerant compressor at variable speed, according to the refrigerant flowrate requirements.
  • Electric power for the electric motor driving an LNG compressor train is gen erated by one or more electric generators, as usually no suitable electric distribution grid is available at the site where the LNG plant is located.
  • a common feature of the above described LNG systems is that an important share of natural gas is used to generate the mechanical power required to drive the compressor trains and to increase the volumetric enthalpic content of the natural gas stream through liquefaction. This has a negative impact on the gas liquefaction rate, since part of the gas is used to generate mechanical power to drive the compressors.
  • fossil fuel consumption for running the liquefaction process also has a nega tive environmental impact, as it generates carbon dioxide.
  • an integrated natural gas lique faction system including an energy conversion system adapted to convert energy from a renewable energy resource into energy that can be used to liquefy natural gas by at least one refrigerant circuit adapted to circulate at least one refrigerant therein, wherein the refrigerant circuit includes at least one refrigerant compressor.
  • the energy conver sion system may include an energy collector to collect energy from the renewable energy resource.
  • an integrated natural gas liq uefaction system (shortly“integrated LNG system”) comprise at least one refrigerant circuit adapted to circulate at least one refrigerant therein, wherein the refrigerant cir cuit includes at least one refrigerant compressor.
  • the integrated natural gas liquefac tion system further includes an energy collector, adapted to collect energy from at least one renewable energy resource.
  • a mechanical power generator of the integrated natu ral gas liquefaction system is adapted to convert energy provided by the energy col lector into mechanical power.
  • the mechanical power generator can be directly or in directly powered by energy from the energy collector. For instance, energy from the energy collector can converted and/or stored for later use by the mechanical power generator.
  • the mechanical power generator is drivingly coupled to the refrigerant com pressor. Energy from the renewable energy resource is thus exploited by the integrated LNG system to drive at least one refrigerant compressor, thus reducing or eliminating the need to bum natural gas or other fossil fuel to drive the refrigerant compressor.
  • the energy collected by the energy collector can be stored temporarily.
  • the collected energy can be converted into one or more different kinds of energy, depending on the nature of the renewable energy resource used, the nature of the energy collector, the manner of storing energy, for instance.
  • the energy collected from the renewable energy resource can be converted, for instance, into electric energy, potential energy, chemical energy, thermal energy (heat), kinetic energy or combinations thereof.
  • an energy collector of the integrated LNG system is any ma chinery aggregation adapted to produce useful energy, such as electrical, mechanical or chemical energy, exploiting a renewable energy resource, such as solar energy, tide energy, wind energy, geothermal energy and the like.
  • the energy collector can include, among others, a concentrated solar power plant, a photovoltaic solar plant, a wind farm, a hydroelectric plant, a tidal or wave energy converting plant, a geothermal plant, or combinations thereof.
  • Energy collected from the renewable energy resource by the energy collector can be made available as electric power to drive one or more compressors of one or more compressor trains of the LNG system by means of one or more electric motors, which convert the electric energy in mechanical energy. For instance, solar or wind energy can be converted into electric energy, which is subsequently converted into mechanical energy by an electric motor to drive a compressor or compressor train.
  • energy collected by the energy collector from the re newable energy resource can be used to produce hydrogen by electrolysis.
  • Hydrogen can then be used, for instance, to fuel an endothermic engine, such as a gas turbine engine, to produce mechanical power and drive a compressor or compressor train adapted to process one or more refrigerants of the integrated LNG system.
  • energy collected by the energy collector from the re newable energy resource can be made available as thermal energy (heat).
  • Heat can be converted into mechanical power to drive the refrigerant compressor. Conversion can be performed through a thermodynamic cycle, e.g. a Rankine cycle using a steam or vapor turbine, or a Brayton cycle, using a gas turbine.
  • the mechanical power is converted in electric energy, which can be converted into mechanical energy or into chemical energy, for instance in hydrogen, which is subsequently used to fuel an endothermic engine, such as a gas turbine engine, to generate mechanical power and drive the refrigerant compressor.
  • Fig. l illustrates a simplified schematic representation of a plant according to the present disclosure in one embodiment
  • Fig.2 illustrates a simplified schematic representation of a plant according to the present disclosure in a further embodiment
  • Fig.3 illustrates a simplified schematic representation of a plant according to the present disclosure in a further embodiment
  • Fig.4A, 4B, 4C and 4D summarize several embodiments of energy storage devices suitable for use in an LNG system according to the present disclosure
  • Figs.5, 6, 7, 8 and 9 illustrate schematics of integrated LNG systems using concentrated solar energy in one embodiment
  • Fig.10 illustrates an LNG system using renewable energy resources to pro prise hydrogen as a fuel for a gas turbine engine
  • Fig.11 illustrates a further LNG system using renewable energy resources to produce hydrogen as a fuel for fuel cells.
  • a novel and useful integrated natural gas liquefaction system has been devel oped.
  • energy from a renewable energy resource at least partly contributes to run one or more refrig erant compressors.
  • the use of energy from renewable energy resources reduces con sumption of natural gas, or other valuable and non-renewable energy resources to run the drivers of the refrigerant compressors.
  • renewable energy resources may not be able to provide the full amount of power needed or may deliver more than the power required to drive the refrigerant compressors
  • measures are adopted to ac cumulate or store surplus of energy delivered by the renewable energy resource for use when insufficient power is delivered by said renewable energy resource.
  • surplus electric energy generated by conversion of renewable energy can be exported into an electric distribution grid.
  • the integrated natural gas liq uefaction system includes at least one refrigerant circuit adapted to circulate at least one refrigerant therein, wherein the refrigerant circuit includes at least one refrigerant compressor driven by a mechanical power generator; and wherein the refrigerant cir cuit is adapted to remove heat from a flow of natural gas.
  • the integrated natural gas liquefaction system includes at least one energy collector, adapted to collect energy from at least one renewable energy resource, such as solar energy or wind energy.
  • the integrated natural gas liquefaction system further includes an energy converter, adapted to convert energy collected by the energy collector into electric energy.
  • the energy converter can include one or more converting devices, which may be identical to one another, or different from one another, for instance, if different renewable en ergy resources are used in combination in the same integrated natural gas liquefaction system.
  • the integrated natural gas liquefaction system may further include an electric distribution grid, adapted to receive electric energy generated by the energy converter.
  • the electric distribution grid is adapted to deliver electric energy to an energy storage system, wherein electric energy is stored in an energy form suitable to be stored.
  • the mechanical power generator includes an electric motor, which is electrically coupled to the electric distribution grid to generate mechanical power and is drivingly coupled to the refrigerant compressor.
  • the integrated natural gas liquefaction system further includes in internal combustion engine, such as a gas turbine engine, adapted to be fueled with natural gas from the flow of natural gas and drivingly coupled to an electric generator.
  • the electric generator is electrically coupled to the electric distribution grid, to provide electric power to the electric motor and/or to the energy storage system, in case of shortage of energy from the storage unit or from the renewable energy resource.
  • Fig.1 illustrates a schematic of a first embodiment of an integrated natural gas liquefaction system (herein shortly re ferred to also as LNG system), labeled 1 as a whole.
  • LNG system natural gas liquefaction system
  • a natural gas liquefaction system comprises one or more compressors or compressor trains, which process one or more refrigerant fluids that are subjected to cyclic thermodynamic transformations.
  • Mechanical power drives one or more refrigerant compressors.
  • the refrigerant fluid at the delivery side of the compressor(s) is cooled and expanded, to reach low temperatures.
  • the expanded refrigerant removes heat from the flow of natural gas by heat exchange therewith.
  • the heated refrigerant gas is com pressed again by the refrigerant compressor(s).
  • the present disclosure concerns an efficient way of using renewable energy resources to run one or more refrigerant compressors in an integrated LNG system.
  • the core of the thermodynamic cycle of the LNG system which processes the one or more refrigerant fluids, includes at least one refrigerant circuit 3.
  • the refrigerant circuit 3 includes at least one refrigerant compressor.
  • compressor 5 is representa tive of one or more compressors or compressor trains to process one or more refriger ant fluids.
  • the refrigerant circuit further comprises a chiller 7, an expander 9 and a heat exchanger 11.
  • the refrigerant delivered by refrigerant compressor 5 is chilled in chiller 7, e.g. in heat exchange relationship with air, water or a further refrigerant of another refrigerant circuit.
  • the compressed and chilled refrigerant is expanded in ex pander 9 to achieve a sufficiently low temperature, such that heat can be removed therewith from a flow of natural gas (NG) delivered by a pipeline 12 and flowing through the heat exchanger 11.
  • NG natural gas
  • LNG liquefied natural gas
  • the refrigerant circuit 3 is just used as a schematic representation of a generic refrigeration system including one or more refrigerant circuits.
  • the structure and operation of the refriger ant circuit per se is not particularly relevant.
  • an im portant aspect is that the refrigeration system includes at least one refrigerant compres sor and a mover for the refrigerant compressor, and that at least part of the power to drive the refrigerant compressor is provided by the renewable energy resource.
  • the refrigerant circuit 3 that is shown only schematically in Fig. l, as well as in the remaining figures, can be configured according to any one of several known refrigeration systems and cycles, or a parts thereof, such as for instance, but without limitation: - a single mixed refrigerant cycle, marketed under the trademark PRICO®;
  • the refrigerant compressor 5 which schematically represent one or more compressor trains for one or more refrigerants, is driven by at least one driver.
  • one or more compressors can be grouped to form one or more compressor trains, each driven by at least one respec tive driver.
  • a driver 17 is driv- ingly coupled to refrigerant compressor 5.
  • the driver is a mechanical power generator, which generates mechanical power to rotate the refrigerant compres sors) 5.
  • the driver 17 can include an electric motor.
  • the electric motor is powered by electric energy from an electric energy source, for instance from an electric distribution grid 19 forming part of the LNG system 1.
  • Electric energy to the electric distribution grid 19 is provided directly or in directly by an energy collector 20, which collects energy from a renewable energy resource.
  • the renewable energy resource is solar radiation, which is converted into electricity by a photovoltaic field 21 comprised of a plurality of photovoltaic panels 23 electrically coupled to the electric distribution grid 19 via an inverter unit 25.
  • the inverter unit 25 can include a single inverter or a plurality of inverters. Hereon the inverter unit 25 will be referred to simply as“inverter”, but this shall not be construed narrowly.
  • the energy collector 20, therefore, includes photo voltaic panels 23 and the inverter 25.
  • a variable frequency drive 27 can be positioned between the inverter 25 and the electric motor 17. In the schematic of Fig.1 the inverter 25 is connected to the variable frequency drive 27 through the electric distribution grid 19.
  • the electric motor 17 can rotate at a rotational speed, which can differ from the frequency of the AC current delivered by the inverter 25, and which can be non constant, to adapt the rotational speed of the refrigerant compressor 5 to the operating conditions of the thermodynamic circuit 3. For instance, if a lower refrigerant flow rate is required, the refrigerant compressor 5 can be driven at lower speed.
  • the amount of energy provided by the renewable energy resource can be sufficient to drive all compressors of the LNG system 1.
  • the renewable energy resource may be used to provide energy to only one or some refrigerant compressors, or only part of the energy required to drive a compressor or a compressor train.
  • one of said drivers can be a driver according to the current art, while the other can be a mechanical power generator, directly or indirectly powered by energy from the energy collector.
  • a share of renewable energy collected by the energy collector 20 can be used also to power other utilities and services in the system, if needed or desirable.
  • the energy collector 20 may provide sufficient power to drive the compressor 5, i.e. all compressors of the LNG system 1, or some of them, e.g. if more than one driver is provided and only one or some of them are intended to be powered by energy from the renewable energy resource.
  • the surplus energy can be stored in an energy storage system 29.
  • This latter can be comprised of one or more energy storage facilities, some of which will be described later on.
  • the energy storage system 29 can include one or more storage facilities suitable for this application, selected among the storage facili ties available.
  • an auxiliary mechanical driver can be provided for directly or indirectly driving the refrigerant compres sors).
  • the auxiliary mechanical driver can be coupled directly to the re frigerant compressor 5 and drive the refrigerant compressor 5 with mechanical power generated by the auxiliary mechanical driver.
  • Hybrid operating conditions can also be foreseen, wherein the compressor or compressor train is driven by power generated by the auxiliary mechanical driver and by power delivered by the energy storage system 29.
  • the auxiliary mechanical driver can drive an electric generator, which converts mechanical power into electric power.
  • the electric power generated by the electric generator driven by the auxiliary mechanical driver can be used to power an electric motor drivingly coupled to the refrigerant compressor 5.
  • Electric power generated by the electric generator driven by the auxiliary mechanical driver can be made available through the electric distribution grid 19 and can be added to electric energy obtained from renewable energy resource through by the energy col lector 20.
  • an auxiliary mechanical driver 31 includes a gas turbine engine 31 , drivingly coupled to an el ectri c generator 33.
  • the gas turbine engine 31 can comprise a compressor section 31.1, a combustor section 31.2 and an expander or turbine section 31.3.
  • the gas turbine engine 31 can be fueled with natural gas NG from the pipeline 12.
  • the LNG system 1 described above and schematically shown in Fig.1 can operate in different modes depending upon the amount of energy available from the renewable energy resource and collected by the energy collector 20, and on the amount of power required to drive the refrigerant compressor 5. As noted above, if energy collector 20 provides more energy than required to drive the refrigerant compressor 5, surplus energy can be stored in the energy storage system 29.
  • energy from the energy storage system 29 can be used to drive the refrigerant compressor 5.
  • energy from the energy storage system 29 can also be used for short time spans, during which the renewable energy resource provides insufficient energy. If no power or insufficient power is available from the renewable energy resource and the shortage cannot be balanced by energy from the energy storage system 29, the auxil obviouslyy mechanical driver 31 is used.
  • the gas turbine engine 31 is started and used to generate electric energy via electric generator 33. The electric energy thus generated is converted into mechanical energy by the electric motor 17 to drive the refrigerant compressor 5.
  • FIG.2 illustrates an LNG system, again labeled 1 as a whole, which includes an energy collector 20 comprised of a wind farm, to convert wind en ergy into electric energy.
  • the wind farm is shown at 22.
  • Wind turbines of wind farm 22 are shown at 24.
  • Reference number 25 designates a converter which can convert the electric energy generated by the wind turbines into electric energy suitable for sup ply on the electric distribution grid 19.
  • the remaining components of the integrated LNG system 1 ofFig.2 are the same as in Fig.1 and are labeled with the same reference numbers. These components will not be described again.
  • FIG.3 An integrated LNG system 1 comprises an energy collector 20 including a field 21 of photovoltaic panels 23 and a further energy collec tor 20 including a wind farm 22.
  • Some components of the LNG system 1 in Fig.3 are the same as in Figs. 1 and 2 and are labeled with the same reference numbers used in Figs. 1 and 2 and are not described again.
  • Inverters or converters 25 convert the electric energy generated by the wind turbines 24 of the wind farm 22 and by the photovoltaic panels 23 of the photovoltaic field 21 into electric energy at the correct frequency and phase for exportation to the electric distribution grid 19.
  • An energy storage system 29 collects surplus energy which may be available from the energy collector 20.
  • the auxiliary mechanical driver 31 comprises a gas turbine engine which can be drivingly coupled to the refrigerant compressor 5 through a shaft line 40 and a clutch 41.
  • a second clutch 43 is arranged along a shaft line 42, which drivingly con nects the electric motor 17 to the refrigerant compressor 5.
  • the clutch 43 can be disengaged and the clutch 41 can be engaged, such that mechanical power from the gas turbine engine 31 can be used to directly drive the refrigerant com pressor 5.
  • both clutches 43 and 41 can be engaged, and mechanical power from the gas turbine engine 31 and from the electric motor 17 can be used in combination to drive the refrigerant compressor 5.
  • the energy storage system 29 can include one or more different storage fa cilities.
  • Fig.4A summarizes some options for energy storage systems 29 to be used in an LNG system according to the present disclosure.
  • the energy storage system 29 can include battery energy storage devices, flow battery energy storage devices, flywheel energy storage devices, supercapacitor energy storage devices, superconducting magnetic en ergy storage devices, or combinations thereof.
  • the electric energy is converted and stored in various forms of energy.
  • batteries including flow batteries, store energy in the form of chemical energy.
  • Flywheel energy storage in volves converting the electric energy in kinetic energy by driving into fast rotation a flywheel, which is arranged in a low-pressure vessel to reduce friction and is supported by low-friction bearings, including a magnetic levitation module, for instance.
  • Super capacitor energy storage systems involve storing electric charges between two con ductive plates separated by a dielectric layer.
  • Superconducting magnetic energy stor age involves storing energy in form of an electric current flowing in coils made of superconductive material and maintained at cryogenic temperature to achieve almost zero resistance and thus reduce or substantially eliminate electric losses.
  • the energy storage system 29 includes a battery 51 and a rectifier 53, which electrically connects the battery to the electric distribution grid 19.
  • FIG.4B a different energy storage sys tem 29 is shown in Fig.4B.
  • This exemplary embodiment includes a cryogenic energy storage system, for instance a liquefied air storage system, also known as LAES sys tem.
  • the energy storage system again labeled 29 as a whole, can include an air com pressor 55 driven by an electric motor 57, which is electrically coupled to the electric distribution grid 19. Surplus of electric energy made available by the energy collector 20 is used to power the electric motor 57.
  • the compressed air delivered by the air compressor 55 is chilled and liquefied and finally collected in a liquid air storage tank 59.
  • air liquefaction is achieved by compressing an air flow by means of air compressor 55, chilling the compressed air flow in heat exchangers 58 A, 58B and expanding the chilled air flow in an expander or in a Joul e-Thomson valve 60.
  • the liquid air is maintained at low temperature in the liquid air storage tank 59.
  • a cryogenic pump 62 delivers a flow of liquefied air through a heater 64 and the pres surized and heated air flow is expanded in an expander 66, for instance a turbo-ex- pander. Mechanical power generated by the expander 66 drives an electric generator 68 and the electric power thus generated is delivered to the electric distribution grid 19 for driving the refrigerant compressor 5 of the integrated LNG system 1.
  • a hydro energy storage system 29 is shown in Fig.4C.
  • the hydro energy storage system can comprise a lower water reservoir 70A and an upper water reservoir 70B.
  • a pipeline 72 connects the lower water reservoir 70A and the upper water reservoir 70B.
  • a reversible pump-turbine 74 arranged in the pipeline 72 is adapted to pump water from the lower reservoir 70 A to the upper reservoir 70B and to be driven into rotation by water flowing in the opposite direction, from the upper reservoir 70B to the lower reservoir 70A.
  • An electric ma chine 76 is drivingly coupled to the reversible pump-turbine 74.
  • the electric machine 76 When the reversible pump-turbine 74 operates in the pumping mode, the electric machine 76 operates in a motor mode and is powered by electric energy from the electric distribution grid 19. The electric energy is thus converted into mechanical energy by the electric machine 76 and in potential hydro energy by the pump-turbine 74.
  • the reversible pump- turbine 74 When the reversible pump- turbine 74 operates in the turbine mode, the potential hydro energy is converted into mechanical energy by the pump-turbine 74 and in electric energy by the electric ma chine 76 operating in a generator mode.
  • the hydro energy storage system may include separate pump and turbine, arranged in separate ducts, one for pumping water from the lower reservoir 70 A to the upper reservoir 70B and the other for flowing water from the upper reservoir 70B to the lower reservoir 70A.
  • a single electric machine adapted to operate in a motor mode and in a generator mode can be provided, and selectively coupled to the pump and to the turbine.
  • separate electric motor and elec tric generator can be drivingly coupled to the pump and to the turbine, respectively.
  • CAES systems Compressed air energy storage systems
  • the CAES system includes an air compressor 80, a cavern 82 and/or a pressurized air tank 83 and a tur bine 84.
  • the air compressor 80 and the turbine 84 are arranged on the same shaftline 86.
  • An electric machine 87 arranged along the shaftline 86 can be connected selectively to the air compressor 80 through a first clutch 88 A and to the turbine 84 through a second clutch 88B.
  • the electric machine 87 operates in an elec tric motor mode and converts electric energy available from the electric distribution grid 19 into mechanical energy, to drive the air compressor 80.
  • Compressed air deliv ered by the air compressor 80 can be cooled in a heat exchanger 89 and accumulated in the cavern 82 and/or in the pressurized air tank 83.
  • the turbine 84 is inoperative and the clutch 88B can be disengaged.
  • the clutch 88A can be disengaged and the clutch 88B can be engaged to connect the electric machine 87 to the turbine 84.
  • the electric machine 87 operates in the generator mode.
  • Compressed air previously stored in cav ern 82 and/or in pressurized air tank 83 is delivered to a combustor 92 where com pressed air can be mixed with a fuel, for instance natural gas form pipeline 12.
  • Combustion gas from the combustor 92 is expanded in turbine 84 to generate mechan ical power which is converted into electric power by the electric machine 87 operating in the generator mode.
  • Exhaust gas from the turbine 84 can be used to preheat the compressed air in a pre-heater 94 arranged upstream of the combustor 92.
  • a variable frequency drive 90 can be connected between the electric machine 87 and the electric distribution grid 19.
  • the energy storage systems 29 illustrated in Figs. 4 A, 4B, 4C, 4D are shown by way of example only. Those skilled in the art of energy storage will understand that other energy storage systems can be used, either alone or in various combinations, in order to store energy surplus generated by the renewable energy resource.
  • the selec tion of the energy storage technology may depend upon several factors, among which environmental conditions, availability of natural or artificial water reservoirs, air tanks or caverns, etc..
  • Energy from the energy storage system 29 can be used either to provide sup plemental energy to cover peak power demand by the refrigerant circuit 3, or to pro vide energy when energy from the renewable energy resource is unavailable, for in stance at night in case of a solar photovoltaic plant, or when no wind blows, in case of a wind farm.
  • solar energy can be exploited by means of a concentrated solar power plant and converted into thermal energy.
  • a concentrated solar power plant Exemplary em bodiments using concentrated solar power plant are shown in Figs 5, 6, 7, 8, 9.
  • an integrated natural gas liquefaction system may include at least one refrigerant circuit adapted to circulate at least one refrigerant therein, wherein the refrigerant circuit includes at least one re frigerant compressor; and wherein the refrigerant circuit is adapted to remove heat from a flow of natural gas.
  • the integrated natural gas liquefaction system further in cludes a concentrated solar power plant, comprised of at least one solar concentrator adapted to concentrate solar radiation. Thermal energy from the solar concentrator is transferred to a thermodynamic cycle, wherein heat from the concentrator is converted into mechanical power by the thermodynamic cycle through a mechanical power gen erator and possibly further converted into electric power.
  • the thermodynamic cycle is therefore an energy converter which may convert energy from the renewable energy resource into another useful form of energy, such as mechanical or electric energy, as disclosed here below.
  • the system may further include a heat storage facility, to store heat from the concentrated solar power plant
  • the system may further include an energy storage system adapted to store electric energy, suitably converted into another form of storageable energy prior to storage.
  • Heat can be transferred directly from the solar concentrator to a working fluid of the thermodynamic cycle.
  • heat is transferred from the solar con centrator to the thermodynamic cycle through an intermediate heat transfer circuit.
  • the mechanical power generator is drivingly coupled to the refrigerant compressor.
  • the integrated natural gas liquefaction system further comprises a first elec- trie machine adapted to be drivingly coupled to the mechanical generator and electri cally coupled to an electric distribution grid.
  • This latter is functionally coupled to an energy storage system, adapted to store surplus energy generated by the mechanical power generator and suitably converted into a storageable form of energy.
  • the integrated natural gas liquefaction system further comprises an auxiliary mechanical driver, such as a combustion engine, for instance, a gas turbine engine, drivingly coupled to a second electric machine, adapted to con vert mechanical power generated by the auxiliary mechanical driver into electric power.
  • an auxiliary mechanical driver such as a combustion engine, for instance, a gas turbine engine, drivingly coupled to a second electric machine, adapted to con vert mechanical power generated by the auxiliary mechanical driver into electric power.
  • the second electric machine is electrically coupled to the electric distribution grid to supply electric power to the first electric machine, for driving the refrigerant compressor, when insufficient power is provided by the mechanical power generator.
  • the auxiliary mechanical driver can include a combustion engine fueled with natural gas, or with hydrogen, or with a combination thereof. Hydrogen can be proucked electrically, exploiting electric power generated by the first electric machine, for instance.
  • the thermodynamic cycle can include a steam or vapor cycle, such as a Ran- kine cycle, or a closed or open gas cycle, such as a Bray ton cycle.
  • a steam or vapor cycle such as a Ran- kine cycle
  • a closed or open gas cycle such as a Bray ton cycle.
  • a heat generator fueled with a suitable fuel, such as natural gas, can be associated to the thermodynamic cycle, for providing additional thermal power to the working fluid, for instance in case insufficient thermal power is provided by the concentrated solar power plant.
  • a heat generator can be used in combination with an open or with a closed thermodynamic cycle.
  • the heat generator can be used, e.g., as a boiler or a re-heater to heat or re-heat a steam or vapor flow in a Rankine cycle, for instance.
  • the heat generator can be used to heat a flow of compressed gas, e.g., in an open or closed Brayton cycle.
  • Figs. 5 to 9 illustrate embodiments of integrated natural gas liquefaction sys tems using concentrated solar power plants.
  • Fig. 5 illustrates an integrated LNG system 1 including a re frigerant circuit 3 adapted to circulate a refrigerant fluid therein.
  • the refrigerant circuit 3 includes a refrigerant compressor 5, a chiller 7, an expander 9 and a heat exchanger 11.
  • the refrigerant delivered by refrigerant compressor 5 is chilled in chiller 7 and expanded in expander 9 to achieve a sufficiently low temperature, such that heat can be removed therewith from natural gas (NG) flowing in pipeline 12.
  • NG natural gas
  • LNG liquefied natural gas
  • the refrigerant circuit 3 and relevant refrigerant compressor 5 are used as simple pictorial representa tion for any kind of refrigerant facility, which may include one or more compressor trains and one or more refrigerant circuits, according to any available LNG technology.
  • an energy collector again labeled 20, is provided to collect solar energy.
  • the energy collector 20 includes a concentrated solar power plant 101.
  • Concentrated solar power plants are known in the art and do not require a detailed description. Only the main components thereof will be mentioned herein.
  • the concentrated solar power plant 101 can include a closed circuit adapted to circulate a heat carrier fluid, which transfers heat from solar concentrators to a thermodynamic circuit, where heat is partly converted into mechanical power.
  • the concentrated solar power plant 101 includes a solar concentrator 103.
  • solar concentrators are known in the art and may be used in the concentrated solar power plant 101.
  • the concentrator 103 includes a plurality of heliostats, such as parabolic mirrors 103 A, for instance.
  • a closed heat carrier fluid circuit 105 transfers heat from the solar concentrator 103 to a thermodynamic circuit 107.
  • thermodynamic circuit is adapted to perform a regenerative Rankine cycle and includes a steam or vapor turbine 109, which may include a high pressure turbine 109 A and a low pressure turbine 109B.
  • the steam or vapor turbine 109 is a mechanical power gen erator, which generates mechanical power to drive the refrigerant compressor 5 of the refrigerant circuit 3 exploiting renewable energy.
  • the process fluid processed through the steam or vapor turbine 109 can be water. In other embod iments, the process fluid can be an organic working fluid.
  • the process fluid circulating in the thermodynamic circuit 107 is heated, va porized and superheated using heat from the closed heat carrier fluid circuit 105, through a heater 111, a vaporizer 113 and a superheater 115.
  • Superheated steam or vapor is partly expanded in the high-pressure turbine 109 A, re-heated in a re-heater 117 and further expanded in the low-pressure turbine 109B.
  • Expanded steam or vapor is condensed in a condenser 1 19 and pumped by a pump 121 again through the heating section of the circuit, including heater 111, vaporizer 113 and superheater 1 15.
  • the thermodynamic circuit 107 can include an auxiliary boiler, wherein heat is generated e.g. by burning natural gas, when insufficient solar power is available, for instance.
  • the boiler can be arranged to supplement thermal energy to one or more of the sections of the closed steam or vapor circuit.
  • the boiler is shown at 123 and is configured to supply regeneration heat. More in general, the boiler can be used to provide supplemental thermal energy to the heater, vaporizer and/or superheater of the steam and/or vapor circuit, whenever no heat or insufficient heat is provided by the concentrator 103.
  • the steam or vapor turbine 109 and the refrigerant com pressor 5 can be arranged on a common shaftline.
  • a clutch 131 can be arranged along the shaftline between the steam or vapor turbine 109 and the refrigerant compressor 5.
  • an electric machine e.g. an electric motor/generator 133 can be drivingly coupled to the steam or vapor turbine 109 and/or to the refrigerant compressor 5.
  • an electric motor/generator 133 is arranged on the same shaftline as the refrigerant compressor 5 and the steam or vapor turbine 109 is drivingly coupled thereto through a clutch 135.
  • the electric motor/generator 133 is electrically coupled to the electric distribution grid 19.
  • the electric distribution grid 19 can be functionally coupled to an energy stor age system 29, as shown in Figs. 1, 2 and 3, not shown in Fig.5.
  • an energy stor age system 29 if the mechanical power generated by the steam or vapor turbine 109 exceeds the needs from refrigerant compressor 5, surplus power can be converted into electric power by electric motor/generator 133, which is operated in the generator mode, and stored in the energy storage system 29.
  • energy from the energy storage system 29 can be used if insufficient heat is available from the concentrated solar power plant 101 and/or from the boiler 123.
  • the integrated LNG system 1 of Fig.5 can further in clude a gas turbine engine 31, similar to the gas turbine engine 31 ofFigs. 1 and 2.
  • the gas turbine engine 31 can be operated to drive an electric generator 33 connected to the electric distribution grid 19, if energy from the concentrated solar power plant 101 and/or from the energy storage system 29 is insufficient and if no boiler 123 is pro vided or if said boiler 123 provides insufficient heat or is temporarily unavailable, for instance.
  • Mechanical power generated by the gas turbine engine 31 is converted into electric energy by the electric generator 33.
  • the electric energy is made available through electric distribution grid 19 to drive the electric motor/generator 133 in the motor mode and drive the refrigerant compressor 5 therewith, either alone or in com bination with the steam or vapor turbine 109.
  • the concentrated solar power plant 101 may also in clude a heat accumulator 102.
  • the concentrated solar power plant 101 uses linear solar con centrators
  • heliostats concentrating solar energy on a receiver placed on top of a tower can be used.
  • the receiver can be part of a closed circuit, wherein a heat transfer fluid circulates.
  • the heat transfer fluid can transfer heat to a working fluid, which converts thermal energy into mechanical energy through a Ran- kine cycle, for instance.
  • concentrated solar power can be converted into me chanical power using a Bray ton cycle.
  • Concentrated solar power can heat a flow of compressed air, which is then expanded in a power turbine.
  • the power turbine generates mechanical power to drive an electric generator.
  • the power turbine can be driv- ingly coupled to an air compressor, e.g. an axial air compressor, which compresses the air which is then heated by means of concentrated solar power.
  • the entire mechanical power generated by the power turbine can be converted into electric energy and the air compressor can be driven by an electric motor.
  • An auxiliary combustor can be provided, to provide heat if the solar energy is insufficient.
  • Fig.6 illustrates a schematic of an integrated LNG system 1 including a re frigerant circuit, again schematically shown at 3, and an energy collector 20, which includes a concentrated solar power plant 101.
  • the refrigerant circuit 3 can be config ured as described above in connection with Figs. 1 and 2, for instance, and will not be described again.
  • the concentrated solar power plant 101 includes a tower 201, on top of which a receiver 203 is installed.
  • Heliostats 205 focus solar radiation on the receiver 203, where a heat transfer fluid flows, for example a molten salt.
  • the receiver 203 forms part of a closed heat transfer circuit 207.
  • the closed heat transfer circuit 207 can include a hot fluid reservoir 209 and a cold fluid reservoir 211.
  • Hot heat transfer fluid from the re DCver 203 is collected in the hot fluid reservoir 209, where solar energy can be stored as thermal energy.
  • Hot heat transfer fluid can circulate from the hot fluid reservoir 209 through a steam or vapor generation system 213 into the cold fluid reservoir 211, wherefrom the exhausted heat transfer fluid flows back to the receiver 203.
  • the steam or vapor generation system 213 can include a superheater 215, an evaporator 217 and pre-heater 219.
  • Hot heat transfer fluid from the hot fluid reservoir flows sequentially through the superheater 215, the evaporator 217 and the pre-heater 219 in heat exchange relationship with a working fluid circulating in a closed circuit 221 where the working fluid undergoes sequential thermodynamic transformations to convert heat into mechanical power.
  • the working fluid circulating in the closed circuit is pre-heated in pre-heater 219, evaporated in evaporator 217 and superheated in su perheater 215.
  • the hot and pressurized working fluid expands sequentially in a high- pressure steam or vapor turbine 223 and in a low-pressure steam or vapor turbine 225.
  • the partly expanded working fluid from the high-pressure steam or vapor turbine 223 can be regenerated in regenerator 221 in heat exchange relationship with the heat trans fer fluid, prior to be further expanded in the low-pressure steam or vapor turbine 225.
  • the spent working fluid exiting the low-pressure steam or vapor turbine 225 is condensed in a condenser 227 and collected in a tank 229, wherefrom condensed working fluid is pumped by pump 231 in the steam or vapor generator system 213 again.
  • the mechanical power generated by the steam or vapor turbines 223 and 225 drives an electric generator 233, which is electrically connected to an electric distribution grid 19.
  • the electric motor 17 of the refrigerant circuit 3 can be powered by electric energy from the electric distribution grid 19.
  • the steam or vapor turbines 223 and 225 can directly drive in rotation the compressor 5 of the refrigerant circuit 3.
  • an auxiliary gas turbine engine 31 can be provided to drive an electric generator electrically connected to the electric distribution grid 19, similarly to the embodiment of Fig.2, to generate electric power if no or insufficient power is generated by generator 233.
  • the auxiliary mechanical driver can include a gas tur bine engine, which can be drivingly coupled, through a clutch for instance, to the re frigerant compressor 5, as shown in the embodiment of Fig.3.
  • a different cycle can be used to convert heat into mechanical power, for instance a Bray ton cycle using a gas turbine engine.
  • FIG. 7 An embodiment of an integrated natural gas liquefaction system using con centrated solar power and a Brayton cycle is illustrated in Fig. 7.
  • the system of Fig. 7 includes at least one refrigerant circuit adapted to circulate at least one refrigerant therein, wherein the refrigerant circuit in cludes at least one refrigerant compressor; and wherein the refrigerant circuit is adapted to remove heat from a flow of natural gas.
  • the integrated natural gas lique faction system further includes a concentrated solar power plant, comprised of at least one solar concentrator adapted to concentrate solar radiation. Thermal energy from the solar concentrator is transferred to a thermodynamic cycle, wherein heat from the con centrator is converted into mechanical power by a gas turbine engine comprised of a working fluid compressor and a working fluid expander. Working fluid compressed by the working fluid compressor is heated by thermal power collected by solar con centrator and the hot, compressed working fluid is expanded in the working fluid ex pander.
  • thermodynamic cycle can be a closed cycle or an open cycle.
  • thermodynamic cycle is an open cycle.
  • thermodynamic cycle is an energy converter which converts energy from the renewable energy resource into another form of useful energy, such as mechanical and/or electric energy.
  • the gas turbine engine is drivingly coupled to the compressor of the refriger ant circuit and may be further drivingly coupled to an electric machine, such as an electric generator or an electric motor/generator.
  • the electric machine is electrically coupled to an electric distribution grid, which may transfer electric power to an energy storage system.
  • the thermodynamic cycle may include a combustor, wherein natural gas or another fuel is used to generate additional thermal power to heat the compressed working fluid prior to expansion in the working fluid expander, in case of shortage from the concentrated solar power plant.
  • the system may further include a heat storage facility, to store heat from the concentrated solar power plant.
  • Fig.7 illustrates an integrated LNG system 1, including a refrigerant circuit 3 which can include the same compo nents as already described above and labeled with the same reference numbers used in the previously mentioned figures.
  • the integrated LNG system 1 further includes an energy collector 20 adapted to collect solar energy.
  • the energy collector 20 comprises a concentrated solar power plant again labeled 101, which includes a tower 201 with a receiver 203 arranged at the upper end of the tower 201.
  • Heliostats 205 focus solar radiation on the receiver 203, where a heat transfer fluid flows, for example a molten salt.
  • the receiver 203 forms part of a closed heat transfer circuit 207.
  • the closed heat transfer circuit 207 includes a hot fluid reservoir 209 and a cold fluid reservoir 211.
  • Hot heat transfer fluid from the receiver 203 is collected in the hot fluid reservoir 209, where solar energy can be stored as thermal energy.
  • Hot heat transfer fluid can circulate from the hot fluid reservoir 209 through an air heater 251 into the cold fluid reservoir 211, wherefrom the exhausted heat transfer fluid flows back to the receiver 203.
  • thermal energy is transferred from the heat transfer fluid circulating in the closed circuit 207 to compressed air, delivered by an air compressor 253.
  • Compressed hot air is expanded in a power turbine 255 and is discharged through a stack 257.
  • the exhaust air can be used to pre-heat the compressed air delivered by the air compressor 253 in a pre-heating heat exchanger 258.
  • the power turbine 255 and the air compressor 253 are mechanically coupled through a shaft 259, such that mechanical power generated by the expansion of the compressed hot air in the power turbine 255 is used to drive the air compressor 253.
  • the additional power generated by the power turbine 255 and which is not required to drive the air compressor 253 is available on an output shaft 261.
  • the power turbine 255, the air compressor 253, the shaft 259 and the air heater 251 form part of a gas turbine engine globally labeled 265, where ambient air performs a Brayton cycle to convert heat, delivered to the air by the heat transfer fluid circulating in the closed circuit 207, into mechanical power available on the output shaft 261.
  • the output shaft 261 is drivingly coupled to the refrigerant compressor 5 of the refrigerant circuit 3, such that mechanical power made available by the gas turbine engine 263 directly drives the refrigerant compressor 5.
  • the output shaft 261 can be mechanically coupled to an electric generator, which provides electric power exported on an electric distribu tion grid 19. Electric energy from the electric energy distribution grid 19 can be used to power an electric motor, which converts the electric power into mechanical power to drive the refrigerant compressor 5, according to an arrangement similar to Fig.1.
  • an electric gen erator 271 can be drivingly coupled to the outputs shaft 261 and electrically connected to the electric distribution grid 19.
  • a combustor 273 can be provided, through which compressed air flows prior to be expanded in the power turbine 255.
  • a fuel for instance natural gas diverted from the pipeline 12, can be mixed to compressed air in the combustor 273 and the air/fuel mixture can be ig nited to generate compressed, high-temperature combustion gas, which is expanded in the power turbine 255.
  • air can be heated directly in the receiver 203 and the closed circuit 207 can be omitted.
  • a heat storage system can be provided, to store any surplus of thermal energy, for instance using reservoirs of a heat storage medium.
  • FIG. 8 a further embodiment of an inte grated LNG system 1 exploiting mechanical power generated by a concentrated solar power plant 101 is illustrated.
  • the same or corresponding elements and components already described with reference to Fig.5 are labeled with the same reference numbers and will not be described again.
  • the electric motor/generator 133 can operate in a generator mode if the mechanical power generated by the steam or vapor turbine 109 exceeds the power needed to drive the refrigerant compressor 5.
  • Electric energy generated by the electric generator 133 can be used to produce hydrogen in a water electrolyzer 141, which can be electrically coupled to the electric distribution grid 19 via a rectifier 143.
  • Hydrogen produced by the electrolyzer 141 can be stored in a hydrogen storage tank 145 and can be used, when so required, as a fuel to power a gas turbine engine 31 (see also Fig.1).
  • a mixture of hydrogen from the hydrogen storage tank 145 and natural gas from natural gas pipeline 12 can be fed to the combustor 31.2 of the gas turbine engine 31.
  • the gas turbine engine 31 can be operated to drive an electric gen erator 33, which provides electric power to the electric distribution grid 19 to power the electric motor/generator 133 when this latter is operated in the motor mode to drive the refrigerant compressor 5.
  • solar power can be used to drive the refrig erant compressor 5 and to further generate electric power if sufficient solar power is available.
  • the electric energy is converted into chemical energy by hydrogen produc tion and stored in the hydrogen storage tank 145.
  • the energy stored in chemical form can be used when no solar power is available for continuity of operation of the refrig erant circuit 3.
  • Hydrogen can be produced also using a different concentrated solar power plant as described above.
  • solar energy is primarily used to generate mechanical power and drive the refrigerant compressor 5 therewith
  • solar energy in other embodi ments solar energy, or energy from another renewable energy resources, can be ex ploited fully to produce hydrogen.
  • This latter can fuel a gas turbine engine to drive the refrigerant compressor 5 of the refrigerant circuit 3.
  • solar en ergy can be converted into chemical energy, stored in the form of hydrogen, by pho- tocatalytic water splitting.
  • hydrogen can be produced by water electrolysis, in which case the solar energy is converted into electric energy either directly in a pho tovoltaic system or using a concentrated solar power plant to generate mechanical power, which is used to drive an electric generator.
  • electric power for the production of hydro gen can be provided by a wind farm.
  • FIG.9 an exemplary embodi ment of an integrated LNG system 1 is illustrated, which includes an energy collector adapted to collect energy from a renewable energy resource, using concentrated solar power to generate hydrogen.
  • the integrated LNG system 1 of Fig.9 includes a concen trated solar power plant 101 as in the embodiments of Figs. 5 or 8.
  • the main compo nents of the concentrated solar power plant 101 are labeled with the same reference numbers as in Figs. 5 and 8 and will not be described again.
  • a different concentrated solar power plant can be used, for instance as disclosed in Figs. 6 and 7.
  • the steam or vapor turbine 109 generates mechan ical power to drive an electric generator 133, which converts the mechanical energy into electric energy delivered to an electrolyzer 141 to produce hydrogen by water electrolysis.
  • the hydrogen thus produced can be stored in a hydrogen storage tank 145 and used to fuel a gas turbine engine 31.
  • the gas turbine engine 31 drives the refrig erant compressor 5 of the refrigerant circuit 3. If needed or desired, natural gas from the pipeline 12 can be used alone or mixed with hydrogen from the hydrogen storage tank 145.
  • solar energy is collected by a concentrated solar power plant 101
  • solar energy can be collected in different ways, for instance by means of a field 21 of photovoltaic panels 23 (Fig.1), to produce electric energy which is then used for hydrogen production by electrolysis.
  • Other energy collectors for collecting energy from a renewable energy resources can be used to generate elec tric energy for electrolytic production of hydrogen, for instance wind turbines of a wind farm 22.
  • Fig.10 illustrates an integrated LNG system 1, wherein the energy collector 20 for collecting energy from a renewable energy resource (here again solar energy) comprises a field 21 photovoltaic panels 23 and wind turbines 24 of a wind farm 22, to generate electric energy delivered through inverters 25 to an electric distribution grid 19. The electric energy thus generated is used to produce hydrogen in an electro lyzer 141. Hydrogen is collected in a hydrogen storage tank 145 to fuel a gas turbine engine 31. As mentioned above, natural gas can be mixed with hydrogen in the com bustor 31.2 or used alone if insufficient or no hydrogen is available from the tank 145. The gas turbine engine 31 drives the refrigerant compressor 5 of the refrigerant circuit 3.
  • a renewable energy resource here again solar energy
  • the energy collector 20 for collecting energy from a renewable energy resource comprises a field 21 photovoltaic panels 23 and wind turbines 24 of a wind farm 22, to generate electric energy delivered through inverters 25 to an electric distribution grid 19.
  • the electric energy thus generated is used to produce hydrogen in an electro lyzer 141
  • Hydrogen produced exploiting power from the renewable energy resource can alternatively be used in fuel cells, adapted to generate electric power.
  • the electric power can in turn be used to power an electric motor adapted to drive the refrigerant compressor(s) 5 of the refrigerant circuit 3.
  • Fig.1 1 illustrates a schematic of a further integrated LNG system 1 including a refrigerant circuit 3 with one or more compressors schematically represented by com pressor 5.
  • the same reference numbers used in Fig.1 1 are used to designate the same or equivalent parts as already disclosed in connection with Fig.10.
  • electricity generated by an energy collector 20, adapted to collect energy from a renewable energy resource is used to produce hydrogen by electrolysis in an electrolyzer 141.
  • the hydrogen thus produced is collected in a hydrogen tank 145, wherefrom hydrogen is fed to a fuel cell system 146.
  • Chemical energy from the hy drogen flow is converted into electrical energy by the fuel cell system 146 and exported to an electric distribution grid 19 via inverter 148 or any other electric energy condi tioning device.
  • the electric distribution grid 19 powers an electric motor 152 drivingly coupled via a clutch 154 to the compressor(s) 5 of the refrigerant circuit 3.
  • a gas tur bine engine 31 can be provided as an auxiliary driver to drive the compressor 5 should no power be available on the electric distribution grid 19.
  • a method for liquefying natural gas in an inte grated natural gas liquefaction system in which at least one refrigerant circuit is inte grated with an energy collector adapted to collect energy from a renewable energy resource.
  • the method includes the step of generating power with energy collected by the energy collector and producing hydrogen using said power in a hydrogen produc tion facility.
  • the method also includes the further step of generating power (either mechanical or electrical, for instance) by means of a power generator fueled with said hydrogen.
  • renewable energy resources can be used.
  • tidal or wave power generation systems may be used, which convert energy from tide or sea waves into other forms of useful power, such as mechanical power or electrical power.
  • the electrical or mechanical power gen erated by the renewable energy resource can be used to drive compressors 5 of the refrigerant circuit 3 and excess power, if available, can be stored as described above.
  • electric energy generated by the renewable energy resource can be used for hydrogen production.
  • the energy collector 20 of an integrated ENG system 1 may include a geothermal plant, wherein geothermal heat is used to generate mechanical power for mechanical drive or electric generation.
  • the mechanical power is used directly to drive compressor(s) 5 of the refrigeration circuit 3.
  • mechanical power can be converted into electric power, which is then used to drive the refrigerant compressor(s) 5 via an electric motor.
  • An integrated natural gas liquefaction system comprising: at least one refrigerant circuit adapted to circulate at least one refrigerant therein, wherein the refrigerant circuit includes at least one refrigerant compres sor;
  • an energy collector adapted to collect energy from at least one renewable energy resource
  • a mechanical power generator adapted to convert energy provided by the energy collector into mechanical power, wherein said mechanical power generator is drivingly coupled to said refrigerant compressor.
  • Clause 2 The system of clause 1, further comprising an energy stor age system, adapted to store energy from the energy collector, and to deliver energy to the mechanical power generator.
  • the energy storage system comprises at least one of the following: a heat storage system; a compressed air energy storage system; a cryogenic energy storage system; an electric energy storage system, including one of a battery arrangement, a super capacitor arrangement, a liquid metal battery arrangement, a redox flow battery; a hydrogen tank.
  • Clause 4 The system of clause 1 or 2 or 3, further comprising an aux iliary mechanical driver adapted to provide auxiliary mechanical power for directly or indirectly driving the refrigerant compressor when power from the mechanical power generator is insufficient.
  • Clause 10 The system of any one of the preceding clauses, further comprising a hydrogen generator directly or indirectly supplied with energy from the energy collector and a hydrogen storage tank adapted to store said hydrogen; wherein the mechanical power generator includes an endothermic engine adapted to be fueled with said hydrogen and generate mechanical power therewith.
  • Clause 11 The system of clause 10, wherein the hydrogen generator includes an electrolyzer, and wherein said electrolyzer is powered by electric energy provided by the energy collector.
  • a method for liquefying natural gas in an integrated natural gas liquefaction system including a refrigeration circuit and an energy collector adapted to collect energy from a renewable energy resource; the method comprising the following steps:
  • Clause 14 The method of clause 12 or 13, further providing the step of generating auxiliary mechanical power with an auxiliary mechanical driver when power from the renewable energy resource is insufficient to drive said refrigerant com pressor.
  • a method for liquefying natural gas in an integrated natural gas liquefaction system comprising a refrigeration circuit including at least one refrig erant compressor and an energy collector adapted to collect energy from a renewable energy resource; the method comprising the following steps:
  • Clause 17 The method of clause 16, wherein the step of driving the refrigerant compressor includes the step of fueling a gas turbine engine with said hy drogen and driving the refrigerant compressor with said gas turbine engine.
  • An integrated natural gas liquefaction system comprising: an energy collector adapted to collect energy from a renewable energy re source;
  • a hydrogen production facility adapted to produce hydrogen thorough en ergy collected by the energy collector from said renewable energy resource;
  • a power generator adapted to be fueled with hydrogen produced by said hydrogen production facility;
  • At least one refrigerant circuit adapted to circulate at least one refrigerant therein, wherein the refrigerant circuit includes at least one refrigerant compres sor driven by power from said power generator.

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engine Equipment That Uses Special Cycles (AREA)
  • Separation By Low-Temperature Treatments (AREA)

Abstract

L'invention concerne un système de liquéfaction de gaz naturel intégré. Le système comprend un circuit de fluide frigorigène conçu pour faire circuler au moins un fluide frigorigène à l'intérieur, le circuit de fluide frigorigène comprenant au moins un compresseur de fluide frigorigène. Un collecteur d'énergie collecte de l'énergie à partir d'au moins une ressource d'énergie renouvelable. Un générateur d'énergie mécanique, couplé par entraînement au compresseur de fluide frigorigène, convertit l'énergie fournie par le collecteur d'énergie en énergie mécanique.
EP20732488.0A 2019-06-07 2020-06-03 Système de liquéfaction de gaz naturel Pending EP3980704A1 (fr)

Applications Claiming Priority (2)

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IT102019000008367A IT201900008367A1 (it) 2019-06-07 2019-06-07 Un sistema di liquefazione di gas naturale
PCT/EP2020/025261 WO2020244809A1 (fr) 2019-06-07 2020-06-03 Système de liquéfaction de gaz naturel

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EP20732487.2A Pending EP3980703A1 (fr) 2019-06-07 2020-06-03 Système de liquéfaction de gaz naturel utilisant de l'énergie renouvelable pour produire de l'hydrogène

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IT202100028562A1 (it) * 2021-11-10 2023-05-10 Nuovo Pignone Tecnologie Srl Power Plant for Controlling the Renewable Energy Use in an LNG Train
IT202100028559A1 (it) * 2021-11-10 2023-05-10 Nuovo Pignone Tecnologie Srl Method of Controlling the Renewable Energy Use in an LNG Train
WO2023205013A1 (fr) * 2022-04-19 2023-10-26 Energy Vault, Inc. Système de génération d'électricité ou d'hydrogène à partir de gaz naturel
IT202200008660A1 (it) * 2022-04-29 2023-10-29 Nuovo Pignone Tecnologie Srl Stazione di compressione a basse emissioni di carbonio con capacità d’uso duale
WO2023232837A1 (fr) * 2022-06-01 2023-12-07 Totalenergies Onetech Installation comprenant des installations de gnl et d'électricité renouvelable comprenant au moins un système de stockage d'énergie thermique
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IT201900008367A1 (it) 2020-12-07
WO2020244808A1 (fr) 2020-12-10
WO2020244809A1 (fr) 2020-12-10
EP3980703A1 (fr) 2022-04-13

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