WO2009083986A2 - Method and system for generating energy with gas - Google Patents

Method and system for generating energy with gas Download PDF

Info

Publication number
WO2009083986A2
WO2009083986A2 PCT/IL2009/000004 IL2009000004W WO2009083986A2 WO 2009083986 A2 WO2009083986 A2 WO 2009083986A2 IL 2009000004 W IL2009000004 W IL 2009000004W WO 2009083986 A2 WO2009083986 A2 WO 2009083986A2
Authority
WO
WIPO (PCT)
Prior art keywords
gas
energy
auxiliary
supply
generating unit
Prior art date
Application number
PCT/IL2009/000004
Other languages
French (fr)
Other versions
WO2009083986A3 (en
Inventor
Yossi Ram
Original Assignee
C.Cogen
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 C.Cogen filed Critical C.Cogen
Priority to EP09700072A priority Critical patent/EP2240667A2/en
Publication of WO2009083986A2 publication Critical patent/WO2009083986A2/en
Publication of WO2009083986A3 publication Critical patent/WO2009083986A3/en

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02CGAS-TURBINE PLANTS; AIR INTAKES FOR JET-PROPULSION PLANTS; CONTROLLING FUEL SUPPLY IN AIR-BREATHING JET-PROPULSION PLANTS
    • F02C6/00Plural gas-turbine plants; Combinations of gas-turbine plants with other apparatus; Adaptations of gas- turbine plants for special use
    • F02C6/14Gas-turbine plants having means for storing energy, e.g. for meeting peak loads
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02CGAS-TURBINE PLANTS; AIR INTAKES FOR JET-PROPULSION PLANTS; CONTROLLING FUEL SUPPLY IN AIR-BREATHING JET-PROPULSION PLANTS
    • F02C7/00Features, components parts, details or accessories, not provided for in, or of interest apart form groups F02C1/00 - F02C6/00; Air intakes for jet-propulsion plants
    • F02C7/22Fuel supply systems
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02CGAS-TURBINE PLANTS; AIR INTAKES FOR JET-PROPULSION PLANTS; CONTROLLING FUEL SUPPLY IN AIR-BREATHING JET-PROPULSION PLANTS
    • F02C9/00Controlling gas-turbine plants; Controlling fuel supply in air- breathing jet-propulsion plants
    • F02C9/48Control of fuel supply conjointly with another control of the plant

Definitions

  • This invention relates to a method and system for generating energy, in particular electricity, by natural gas.
  • Electric power production and distribution networks need to respond to power demand that varies over time.
  • the demand pattern has a daily, weekly and annual cycles and the electric power production needs to have a generation capacity to meet peak demands. It is clear that the value of the generated electric power is highest at times of peak demand, for example at early evening hours, at times of extreme heat or cold wave, etc.
  • the present invention provides a method and system for generating energy from natural gas supplied through a gas piping system.
  • the method and system of the invention permit to match the rate of gas feed to an energy-generating plant to meet different energy demand needs.
  • the system permits an increase in the rate of gas feed at times of peak energy demand.
  • the ability to increase the rate of gas feed to an energy-generating station is done, in accordance with the invention, without a need to design a piping system adapted to supply gas at a rate to meet peak demands.
  • an auxiliary, compressed natural gas (CNG) system is provided.
  • gas from the gas piping system is fed to the auxiliary gas supply system, is compressed and the CNG is then stored until need.
  • gas to the energy-generating plant may be fed from said auxiliary system, instead of or in addition to gas fed directly from the piping system.
  • a preferred, albeit a non-exclusive type of energy generating in accordance with the present invention is electric energy.
  • an auxiliary CNG supply system comprises: (i) high pressure gas compressors units (for compressing the gas supplied by the gas piping system, typically having a pressure of about 60-80 bar, up to a relatively high storage pressure of about 250 bars) (ii) a high pressure gas storage subsystem, (iii) a gas feed linked to said supply piping system and adapted to feed compressed gas into said storage subsystem, (iv) an auxiliary piping system for feeding gas from the storage sub-system to the energy-generating unit, and (v) a valving subsystem to control gas feed from the gas storage sub-system to the auxiliary piping system.
  • the valving subsystem is operated to supply gas from the auxiliary gas system to the energy- generating unit to power the said unit.
  • the energy generating unit is fed with the gas piping system and from the auxiliary CNG supply system, concomitantly.
  • the present invention provides a system for generating energy by the use of natural gas-operated energy-generating plant.
  • the energy-generating plant is fed by a natural gas-piping system that transports gas from a gas source.
  • the system comprises an auxiliary CNG supply system that comprises (i) high pressure gas compressor unit (ii) a high pressure gas storage subsystem, (iii) a gas feed linked to said supply piping system and adapted to feed compressed gas into said storage subsystem, (iv) an auxiliary piping system for feeding gas from the storage sub-system to the energy- generating unit, and (v) a valving subsystem to control gas feed from the gas storage subsystem to the auxiliary piping system.
  • a control module is included for operating the valving subsystem to supply gas from the auxiliary gas system to the energy-generating unit at times of peak energy demand.
  • the auxiliary CNG supply system In addition to being able to provide auxiliary gas supply to permit a total gas supply at times of peak demands, the auxiliary CNG supply system also permits a limited back-up for supply of gas to the power plant at times where the natural gas piping system is malfunctioning.
  • Fig. 1 is a block diagram of a system in accordance with the invention.
  • the system components are referred to each in the singular. It should, however, be understood that it is meant to refer also to a system with two or a plurality of such components.
  • the gas supply line may in fact be comprised of a number of such lines or pipes.
  • the term "line" in this regards refers to a functionality of transporting gas through one or more pipes than a single component.
  • the ingress and egress gas lines may each include one, two or a plurality of pipes.
  • the system generally designated 100 includes a piping system 102 that transports natural gas from a gas source (not shown) and feeds the gas to the energy-generating plant, in this case an electricity-generating power plant 104.
  • the plant includes one or more turbines (or engines).
  • the natural gas can be fed directly from the piping system 102 to the gas power plant 104, typically through a filter system 108, a metering system 110 and a pressure regulating system 112 of one or more a gas supply lines 106.
  • natural gas is transported, typically at a pressure in the range of between about 60 to 90 bar.
  • the natural gas is fed into the filter system 108 which filters out particulate matter and condensate liquid, typically via a separator in a one or two-stage design, which is known per se.
  • the separator condensate can be collected, stored in vessels and then transported away, e.g. by trucks and disposed.
  • the metering system 110 serves to gauge the amount of utilized natural gas.
  • the design of metering system 110 depends, as known, on the energy-generating capacity of the electric power generating plant 104, or in other words on the intended natural gas flow rate.
  • the design of a metering system is generally known per se and need not be elaborated herein.
  • the regulating system 112 serves for reducing the gas pressure from the supply pressure, typically in the range of between about 60 to 90 bar, to a lower pressure, typically in the range of between about 0.5 to 40 bar in which the natural gas is supplied to the turbines ⁇ engines of the power plant 104.
  • the regulating system 112 may also include a gas preheating arrangement, which may, for example be gas/water pre- heaters known per se. The pressure regulated and optionally preheated gas is then fed to power plant 104 through the gas supply line 106.
  • an auxiliary gas supply system 120 includes an ingress control valve situated on an ingress gas line 124 and an egress control valve 126 on egress gas line 128 for feeding gas from the auxiliary CNG supply system to the power plant 104.
  • Valves 122 and 126 are typically motor-operated valves.
  • the auxiliary CNG supply system 120 also includes a compressor 130, a CNG storage sub-system 132, a regulating system 133, a flow controller 134 and a system control unit 136.
  • the compressor 130 functions to compress the natural gas from its supply pressure, typically in the range of between about 60 to about 90 bar, to a higher pressure, usually in the range of between about 100 to about, 300 bar, typically above 200 bar.
  • the compressor may be water cooled.
  • the compressor may be associated with a gas filtering unit (not shown) for filtering liquid and particulate matter.
  • the storage sub-system 132 may include one or more or even a bank of storage tanks for storing high pressure CNG.
  • the CNG storage capacity of the storage subsystem 132 is designed so as to be able to provide gas in access to that provided through supply lime 106 so as to provide sufficient gas to power plant 104 at times of peak demand.
  • at times of peak electric power demand gas may be fed to power plant 104 jointly from supply line 106 and from auxiliary gas supply system 120 (through egress gas lines 128).
  • the storage sub-system 132 includes more than one tank, their use may be modular to modulate the amount of stored CNG. For example, at times when peak demand for electric power may be expected, e.g. in peak summer or peak winter, all tanks may be used to their full capacity. At other times, only part of the tanks may be used.
  • the auxiliary CNG supply system can also serve as an emergency back-up for use at such times where natural gas supply through the piping system is interrupted.
  • the regulating system 133 serves for reducing the CNG pressure, which is typically in the range of between about 100 to 300 bar, to a lower pressure, typically in the range of between about 0.5 to 40 bar.
  • the regulating system 133 may also include a gas preheating arrangement, which may, for example be gas/water pre-heaters known per se.
  • control module 136 which is coupled to flow meter 138 that measures the amount of gas flow into line 106 through regulating systems 112 and 133, to flow controller 134, to valves 122 and 126 and to compressor 130.
  • valve 122 At times of relatively low electric power demand, e.g. at night, the control module opens valve 122 and induces operation of compressor 130 to thereby store high pressure compressed natural gas (CNG ) in storage sub-system 132. This is in parallel to ongoing gas feed directly from piping system 102 through feed line 106 to power plant 104. At such, storage operation mode, valve 126 is usually closed.
  • CNG compressed natural gas
  • control module switches system 120 into an auxiliary gas supply mode in which valve 126 opens and flow controller is activated to supply gas to plant 104 through gas egress line 128.
  • gas is supplied to power plant 104 both directly from piping system 102 through line 106 as well as from auxiliary CNG supply system 120 via line 128. It is also possible, by some embodiments to feed gas to power plant 104 during the auxiliary CNG supply operational mode only from the auxiliary gas supply system. This may be the case, for example, at times of interruptions in gas supply from piping system 102.
  • control module 136 controls flow controller 134 so as to match the amount of gas supplied by the auxiliary supply system and the gas pressure, to that egressing from regulating systems 112 and 133.

Abstract

The invention relates to a system and a method for generating energy by the use of natural gas-operated energy-generating plant, capable of meeting different energy demand needs.

Description

METHOD AND SYSTEM FOR GENERATING ENERGY WITH GAS
FIELD OF THE INVENTION
This invention relates to a method and system for generating energy, in particular electricity, by natural gas.
BACKGROUND OF THE INVENTION
Electric power production and distribution networks need to respond to power demand that varies over time. The demand pattern has a daily, weekly and annual cycles and the electric power production needs to have a generation capacity to meet peak demands. It is clear that the value of the generated electric power is highest at times of peak demand, for example at early evening hours, at times of extreme heat or cold wave, etc.
Since electricity is a commodity that cannot be stored in its raw form, an electric power generating system has to be engineered for capacities to meet peak power demands. In particular, the fuel supply system for power plants needs to be designed to be able to supply the large amount of fuel needed to power the plant at such times.
The use of gas for fueling power stations is increasing. Natural gas is typically transported through pipes to sites in which it is utilized, such as a power plant. The common practice, in natural gas-operated power stations, is to feed the gas directly to the generators to power the plant. The amount of natural gas that can be fed into a power plant is of course dependent on the transport capacity of the supply pipe, which is in turn limited primarily by the pipe's diameter (a gas flow can of course be increased by increasing pressure, but supply pipes typically work within a certain defined working pressure range of about 60-80 bars). Thus, in order to be able to provide for high rates of fuel supply to meet peak electric energy demand, the pipe needs to have a sufficient diameter therefor. This factor, as can be appreciated, increases the complexity as well as the costs of the supply system. SUMMARY OF THE INVENTION
The present invention provides a method and system for generating energy from natural gas supplied through a gas piping system. The method and system of the invention permit to match the rate of gas feed to an energy-generating plant to meet different energy demand needs. In particular, the system permits an increase in the rate of gas feed at times of peak energy demand. The ability to increase the rate of gas feed to an energy-generating station is done, in accordance with the invention, without a need to design a piping system adapted to supply gas at a rate to meet peak demands. Rather, according to the invention an auxiliary, compressed natural gas (CNG) system is provided. At times other than times of peak demand, gas from the gas piping system is fed to the auxiliary gas supply system, is compressed and the CNG is then stored until need. At times of peak demand, gas to the energy-generating plant may be fed from said auxiliary system, instead of or in addition to gas fed directly from the piping system.
A preferred, albeit a non-exclusive type of energy generating in accordance with the present invention is electric energy.
According to one aspect of the invention there is provided a method for generating energy by a natural gas-operated energy-generating plant. According to the method of the invention an auxiliary CNG supply system is provided that comprises: (i) high pressure gas compressors units (for compressing the gas supplied by the gas piping system, typically having a pressure of about 60-80 bar, up to a relatively high storage pressure of about 250 bars) (ii) a high pressure gas storage subsystem, (iii) a gas feed linked to said supply piping system and adapted to feed compressed gas into said storage subsystem, (iv) an auxiliary piping system for feeding gas from the storage sub-system to the energy-generating unit, and (v) a valving subsystem to control gas feed from the gas storage sub-system to the auxiliary piping system. At times of peak energy demand, the valving subsystem is operated to supply gas from the auxiliary gas system to the energy- generating unit to power the said unit. Typically, at times of such peak demand, the energy generating unit is fed with the gas piping system and from the auxiliary CNG supply system, concomitantly. By another aspect the present invention provides a system for generating energy by the use of natural gas-operated energy-generating plant. The energy-generating plant is fed by a natural gas-piping system that transports gas from a gas source. The system comprises an auxiliary CNG supply system that comprises (i) high pressure gas compressor unit (ii) a high pressure gas storage subsystem, (iii) a gas feed linked to said supply piping system and adapted to feed compressed gas into said storage subsystem, (iv) an auxiliary piping system for feeding gas from the storage sub-system to the energy- generating unit, and (v) a valving subsystem to control gas feed from the gas storage subsystem to the auxiliary piping system. A control module is included for operating the valving subsystem to supply gas from the auxiliary gas system to the energy-generating unit at times of peak energy demand.
In addition to being able to provide auxiliary gas supply to permit a total gas supply at times of peak demands, the auxiliary CNG supply system also permits a limited back-up for supply of gas to the power plant at times where the natural gas piping system is malfunctioning.
BRIEF DESCRIPTION OF THE DRAWINGS
In order to understand the invention and to see how it may be carried out in practice, embodiments will now be described, by way of non-limiting example only, with reference to the accompanying drawing, in which:
Fig. 1 is a block diagram of a system in accordance with the invention.
DETAILED DESCRIPTION OF EMBODIMENTS
In the following, the system components are referred to each in the singular. It should, however, be understood that it is meant to refer also to a system with two or a plurality of such components. For example, the gas supply line may in fact be comprised of a number of such lines or pipes. The term "line" in this regards refers to a functionality of transporting gas through one or more pipes than a single component. Similarly, the ingress and egress gas lines may each include one, two or a plurality of pipes. Also, there may be one or more storage sub-systems, flow controllers, valves, etc. Reference is made to Fig. 1, showing a schematic depiction of a system in accordance with an embodiment of the invention. The system generally designated 100 includes a piping system 102 that transports natural gas from a gas source (not shown) and feeds the gas to the energy-generating plant, in this case an electricity-generating power plant 104. The plant includes one or more turbines (or engines). As generally known in the art, the natural gas can be fed directly from the piping system 102 to the gas power plant 104, typically through a filter system 108, a metering system 110 and a pressure regulating system 112 of one or more a gas supply lines 106.
In the piping system 102, natural gas is transported, typically at a pressure in the range of between about 60 to 90 bar. The natural gas is fed into the filter system 108 which filters out particulate matter and condensate liquid, typically via a separator in a one or two-stage design, which is known per se. As known, the separator condensate can be collected, stored in vessels and then transported away, e.g. by trucks and disposed.
The metering system 110 serves to gauge the amount of utilized natural gas. The design of metering system 110 depends, as known, on the energy-generating capacity of the electric power generating plant 104, or in other words on the intended natural gas flow rate. The design of a metering system is generally known per se and need not be elaborated herein.
The regulating system 112 serves for reducing the gas pressure from the supply pressure, typically in the range of between about 60 to 90 bar, to a lower pressure, typically in the range of between about 0.5 to 40 bar in which the natural gas is supplied to the turbines\ engines of the power plant 104. As known, the regulating system 112 may also include a gas preheating arrangement, which may, for example be gas/water pre- heaters known per se. The pressure regulated and optionally preheated gas is then fed to power plant 104 through the gas supply line 106.
Provided in accordance with the invention is an auxiliary gas supply system 120. It includes an ingress control valve situated on an ingress gas line 124 and an egress control valve 126 on egress gas line 128 for feeding gas from the auxiliary CNG supply system to the power plant 104. Valves 122 and 126 are typically motor-operated valves. The auxiliary CNG supply system 120 also includes a compressor 130, a CNG storage sub-system 132, a regulating system 133, a flow controller 134 and a system control unit 136.
The compressor 130 functions to compress the natural gas from its supply pressure, typically in the range of between about 60 to about 90 bar, to a higher pressure, usually in the range of between about 100 to about, 300 bar, typically above 200 bar. The compressor may be water cooled. The compressor may be associated with a gas filtering unit (not shown) for filtering liquid and particulate matter.
The storage sub-system 132 may include one or more or even a bank of storage tanks for storing high pressure CNG. The CNG storage capacity of the storage subsystem 132 is designed so as to be able to provide gas in access to that provided through supply lime 106 so as to provide sufficient gas to power plant 104 at times of peak demand. As will also be explained further bellow, at times of peak electric power demand gas may be fed to power plant 104 jointly from supply line 106 and from auxiliary gas supply system 120 (through egress gas lines 128). Where the storage sub-system 132 includes more than one tank, their use may be modular to modulate the amount of stored CNG. For example, at times when peak demand for electric power may be expected, e.g. in peak summer or peak winter, all tanks may be used to their full capacity. At other times, only part of the tanks may be used.
In addition to being able to support energy demands and hence peak gas supply demands, the auxiliary CNG supply system can also serve as an emergency back-up for use at such times where natural gas supply through the piping system is interrupted.
The regulating system 133 serves for reducing the CNG pressure, which is typically in the range of between about 100 to 300 bar, to a lower pressure, typically in the range of between about 0.5 to 40 bar. As known, the regulating system 133 may also include a gas preheating arrangement, which may, for example be gas/water pre-heaters known per se.
The operation of the system is controlled by control module 136, which is coupled to flow meter 138 that measures the amount of gas flow into line 106 through regulating systems 112 and 133, to flow controller 134, to valves 122 and 126 and to compressor 130.
At times of relatively low electric power demand, e.g. at night, the control module opens valve 122 and induces operation of compressor 130 to thereby store high pressure compressed natural gas (CNG ) in storage sub-system 132. This is in parallel to ongoing gas feed directly from piping system 102 through feed line 106 to power plant 104. At such, storage operation mode, valve 126 is usually closed.
Once electric power demand increases, control module switches system 120 into an auxiliary gas supply mode in which valve 126 opens and flow controller is activated to supply gas to plant 104 through gas egress line 128. In a typical auxiliary CNG supply operational mode, gas is supplied to power plant 104 both directly from piping system 102 through line 106 as well as from auxiliary CNG supply system 120 via line 128. It is also possible, by some embodiments to feed gas to power plant 104 during the auxiliary CNG supply operational mode only from the auxiliary gas supply system. This may be the case, for example, at times of interruptions in gas supply from piping system 102.
During auxiliary gas supply operational mode, in which gas is supplied to power plant 104 both directly from piping system 102 and from auxiliary supply system 120, control module 136 controls flow controller 134 so as to match the amount of gas supplied by the auxiliary supply system and the gas pressure, to that egressing from regulating systems 112 and 133.

Claims

CLAIMS:
1. A method for generating energy by the use of natural gas-operated energy- generating plant, comprising:
(a) powering the energy-generating unit by gas supplied directly from a piping system that transports natural gas from a gas source and feeds the gas to the energy-generating unit;
(b) providing an auxiliary compressed natural gas (CNG) supply system that comprises (i) a high pressure gas compressors units, (ii) a gas storage subsystem, (iii) a gas feed linked to said supply piping system and adapted to feed compressed gas into said storage subsystem, (iv) an auxiliary piping system for feeding gas from the storage sub-system to the energy-generating unit, and (v) a valving subsystem to control gas feed from the gas storage sub-system to the auxiliary piping system; and
(c) at times of peak energy demand, operating the valving subsystem to supply gas from the auxiliary CNG system to the energy-generating unit to power the said unit.
2. A method according to claim 1, wherein said energy is electric energy and said energy-generating unit comprises one or more gas-operated turbines or engines.
3. A method according to claim 1 or 2, wherein the gas feed comprises a compressor for compressing the gas fed into the CNG storage subsystem.
4. A method according to any one of claims 1-3, wherein at times of peak energy demand feeding gas to the energy-generating unit concomitantly from the gas supply piping system and from the auxiliary CNG supply system.
5. A system for generating energy by the use of natural gas-operated energy- generating plant, comprising:
(a) a piping system that transports natural gas from a gas source and feeds the gas directly to the energy-generating unit; (b) an auxiliary CNG supply system that comprises (i) a high pressure gas compressors units, (ii) a gas storage subsystem, (ii) a gas feed linked to said supply piping system and adapted to feed compressed gas into said storage subsystem, (iii) an auxiliary piping system for feeding gas from the storage sub-system to the energy-generating unit, and (iv) a valving subsystem to control gas feed from the gas storage sub-system to the auxiliary piping system; and
(c) a control module for operating the valving subsystem to supply gas from the auxiliary gas system to the energy-generating unit at times of peak energy demand.
6. A system according to claim 5, wherein said energy is electric energy and said energy-generating unit comprises one or more gas-operated turbines or engines.
7. A system according to claim 5 or 6, wherein the gas feed comprises a compressor for compressing the gas fed into the gas storage subsystem.
8. A system according to any one of claims 5-7, adapted for feeding gas to the energy generating unit concomitantly from the gas supply piping system and from the auxiliary supply system.
PCT/IL2009/000004 2008-01-03 2009-01-01 Method and system for generating energy with gas WO2009083986A2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
EP09700072A EP2240667A2 (en) 2008-01-03 2009-01-01 Method and system for generating energy with gas

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
IL188585A IL188585A0 (en) 2008-01-03 2008-01-03 Method and system for generating energy with gas
IL188585 2008-01-03

Publications (2)

Publication Number Publication Date
WO2009083986A2 true WO2009083986A2 (en) 2009-07-09
WO2009083986A3 WO2009083986A3 (en) 2010-03-11

Family

ID=40326395

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/IL2009/000004 WO2009083986A2 (en) 2008-01-03 2009-01-01 Method and system for generating energy with gas

Country Status (3)

Country Link
EP (1) EP2240667A2 (en)
IL (1) IL188585A0 (en)
WO (1) WO2009083986A2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105422182A (en) * 2015-12-13 2016-03-23 北京工业大学 Pressurization system based on free piston expansion/compressor-linear motor

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5685155A (en) * 1993-12-09 1997-11-11 Brown; Charles V. Method for energy conversion
US5634340A (en) * 1994-10-14 1997-06-03 Dresser Rand Company Compressed gas energy storage system with cooling capability
US6516616B2 (en) * 2001-03-12 2003-02-11 Pomfret Storage Comapny, Llc Storage of energy producing fluids and process thereof

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105422182A (en) * 2015-12-13 2016-03-23 北京工业大学 Pressurization system based on free piston expansion/compressor-linear motor

Also Published As

Publication number Publication date
EP2240667A2 (en) 2010-10-20
IL188585A0 (en) 2008-11-03
WO2009083986A3 (en) 2010-03-11

Similar Documents

Publication Publication Date Title
Peñate et al. Assessment of a stand-alone gradual capacity reverse osmosis desalination plant to adapt to wind power availability: A case study
CN101240947B (en) Self-adapting solar energy heat collection molten salt receiver system
US20030170516A1 (en) Hydrogen based energy storage apparatus and method
US9212568B2 (en) Control system for matching the output of a steam turbine to a changed load
KR101338573B1 (en) Apparatus for supplying vaporized gas fuel
JP2003282122A (en) Energy storage and recovery system and its use method
KR20120126754A (en) Apparatus for supplying vaporized gas fuel of Dual fuel engine type
KR101111702B1 (en) Seawater desalination system control method according to reverse osmosis
US20220220621A1 (en) Method and system for an off-grid variable state hydrogen refueling infrastructure
KR20120126756A (en) Apparatus for supplying vaporized gas fuel of Dual fuel engine type
CN111271750A (en) Coal fired power plant frequency modulation peak shaving system based on heat accumulator
US7316859B2 (en) Storage system and method for supplying hydrogen to a polymer membrane fuel cell
CN219974677U (en) Pipeline pressure control and power generation system
WO2009083986A2 (en) Method and system for generating energy with gas
US11319876B2 (en) Compressed air energy storage power generation apparatus
CN116123521A (en) Ultra-high pressure steam boiler system utilizing valley electricity to store heat and regulation and control method
US4682620A (en) Clean-gas continuous-flow intermediate storage or accumulator plant
CN207740054U (en) A kind of pressure and temperature reducing formula steam waste heat electricity generation system
EP3839321B1 (en) Installation for compensating fluctuations in gas demand in natural gas networks and the method of implementing this compensation
CN211781360U (en) Coal fired power plant frequency modulation peak shaving device based on heat accumulator
CN114033512A (en) Thermoelectric water combined system suitable for large pressurized water reactor nuclear power unit and production process
CN107764121B (en) Energy-saving consumption-reducing system and adjusting method for low-temperature liquefied hydrocarbon storage and transportation station
CN203927874U (en) A kind of steam accumulator system
CN216743828U (en) Energy-saving air separation back-up nitrogen device
CN218237439U (en) Pressure-reducing water supply system for water supply of high-pressure boiler

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 09700072

Country of ref document: EP

Kind code of ref document: A2

NENP Non-entry into the national phase

Ref country code: DE

WWE Wipo information: entry into national phase

Ref document number: 1471/MUMNP/2010

Country of ref document: IN

WWE Wipo information: entry into national phase

Ref document number: 2009700072

Country of ref document: EP