US20150152884A1 - High pressure ratio compressors with multiple intercooling and related methods - Google Patents

High pressure ratio compressors with multiple intercooling and related methods Download PDF

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Publication number
US20150152884A1
US20150152884A1 US14/405,855 US201314405855A US2015152884A1 US 20150152884 A1 US20150152884 A1 US 20150152884A1 US 201314405855 A US201314405855 A US 201314405855A US 2015152884 A1 US2015152884 A1 US 2015152884A1
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compressor
gas flow
chambers
chamber
pressure
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US14/405,855
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Denis Guillaume Guenard
Andrea Gabbrielli
Remo Tacconelli
Nicola Banchi
Giorgio Greco
Fabio Bozzone
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Nuovo Pignone SRL
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Nuovo Pignone SRL
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Assigned to NUOVO PIGNONE SRL reassignment NUOVO PIGNONE SRL ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: GUENARD, Denis Guillaume, TACCONELLI, REMO, BANCHI, NICOLA, BOZZONE, Fabio, GABRIELLI, ANDREA, Greco, Giorgio
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04DNON-POSITIVE-DISPLACEMENT PUMPS
    • F04D17/00Radial-flow pumps, e.g. centrifugal pumps; Helico-centrifugal pumps
    • F04D17/08Centrifugal pumps
    • F04D17/10Centrifugal pumps for compressing or evacuating
    • F04D17/12Multi-stage pumps
    • F04D17/122Multi-stage pumps the individual rotor discs being, one for each stage, on a common shaft and axially spaced, e.g. conventional centrifugal multi- stage compressors
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04DNON-POSITIVE-DISPLACEMENT PUMPS
    • F04D29/00Details, component parts, or accessories
    • F04D29/58Cooling; Heating; Diminishing heat transfer
    • F04D29/582Cooling; Heating; Diminishing heat transfer specially adapted for elastic fluid pumps
    • 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
    • F02C6/04Gas-turbine plants providing heated or pressurised working fluid for other apparatus, e.g. without mechanical power output
    • F02C6/06Gas-turbine plants providing heated or pressurised working fluid for other apparatus, e.g. without mechanical power output providing compressed gas
    • 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
    • F02C7/12Cooling of plants
    • F02C7/14Cooling of plants of fluids in the plant, e.g. lubricant or fuel
    • F02C7/141Cooling of plants of fluids in the plant, e.g. lubricant or fuel of working fluid
    • F02C7/143Cooling of plants of fluids in the plant, e.g. lubricant or fuel of working fluid before or between the compressor stages
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04DNON-POSITIVE-DISPLACEMENT PUMPS
    • F04D17/00Radial-flow pumps, e.g. centrifugal pumps; Helico-centrifugal pumps
    • F04D17/08Centrifugal pumps
    • F04D17/10Centrifugal pumps for compressing or evacuating
    • F04D17/12Multi-stage pumps
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04DNON-POSITIVE-DISPLACEMENT PUMPS
    • F04D29/00Details, component parts, or accessories
    • F04D29/58Cooling; Heating; Diminishing heat transfer
    • F04D29/582Cooling; Heating; Diminishing heat transfer specially adapted for elastic fluid pumps
    • F04D29/5826Cooling at least part of the working fluid in a heat exchanger
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04DNON-POSITIVE-DISPLACEMENT PUMPS
    • F04D29/00Details, component parts, or accessories
    • F04D29/60Mounting; Assembling; Disassembling
    • F04D29/62Mounting; Assembling; Disassembling of radial or helico-centrifugal pumps
    • F04D29/624Mounting; Assembling; Disassembling of radial or helico-centrifugal pumps especially adapted for elastic fluid pumps
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/0002Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the fluid to be liquefied
    • F25J1/0022Hydrocarbons, e.g. natural gas
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/02Processes 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
    • F25J1/0243Start-up or control of the process; Details of the apparatus used; Details of the refrigerant compression system used
    • F25J1/0257Construction and layout of liquefaction equipments, e.g. valves, machines
    • F25J1/0274Retrofitting or revamping of an existing liquefaction unit
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/02Processes 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
    • F25J1/0243Start-up or control of the process; Details of the apparatus used; Details of the refrigerant compression system used
    • F25J1/0279Compression of refrigerant or internal recycle fluid, e.g. kind of compressor, accumulator, suction drum etc.
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/02Processes 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
    • F25J1/0243Start-up or control of the process; Details of the apparatus used; Details of the refrigerant compression system used
    • F25J1/0279Compression of refrigerant or internal recycle fluid, e.g. kind of compressor, accumulator, suction drum etc.
    • F25J1/0281Compression 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
    • F25J1/0283Gas turbine as the prime mechanical driver
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/02Processes 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
    • F25J1/0243Start-up or control of the process; Details of the apparatus used; Details of the refrigerant compression system used
    • F25J1/0279Compression of refrigerant or internal recycle fluid, e.g. kind of compressor, accumulator, suction drum etc.
    • F25J1/0294Multiple compressor casings/strings in parallel, e.g. split arrangement
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F05INDEXING SCHEMES RELATING TO ENGINES OR PUMPS IN VARIOUS SUBCLASSES OF CLASSES F01-F04
    • F05DINDEXING SCHEME FOR ASPECTS RELATING TO NON-POSITIVE-DISPLACEMENT MACHINES OR ENGINES, GAS-TURBINES OR JET-PROPULSION PLANTS
    • F05D2230/00Manufacture
    • F05D2230/80Repairing, retrofitting or upgrading methods
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2230/00Processes or apparatus involving steps for increasing the pressure of gaseous process streams
    • F25J2230/06Adiabatic compressor, i.e. without interstage cooling
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2230/00Processes or apparatus involving steps for increasing the pressure of gaseous process streams
    • F25J2230/20Integrated compressor and process expander; Gear box arrangement; Multiple compressors on a common shaft
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T29/00Metal working
    • Y10T29/49Method of mechanical manufacture
    • Y10T29/49229Prime mover or fluid pump making
    • Y10T29/49236Fluid pump or compressor making
    • Y10T29/49238Repairing, converting, servicing or salvaging

Definitions

  • Embodiments of the subject matter disclosed herein generally relate to high pressure ratio compressors with multiple intercooling and related methods; more particularly, to a turbo-compressor/generator train using a high pressure compressor with multiple intercooling instead of plural compressors.
  • turbo-machinery is a centrifugal compressor.
  • Centrifugal compressors are usually designed in families intended to cover a specific flow range and use.
  • a centrifugal compressor may be arranged to perform compression one after another.
  • two centrifugal compressors are typically arranged in a turbo-compressor/generator train 100 as illustrated in FIG. 1 .
  • Such turbo-compressor/generator trains may be used for blast furnaces in the steel industry, natural gas liquefaction, gas reinjection and other oil and gas services.
  • a gas turbine 110 a generator 120 , a gear box 130 , a first low pressure compressor 140 , and a second compressor 150 .
  • This type of arrangement is sometimes called a “single-shaft” configuration.
  • the generator 120 may have a rotation speed of 3000 rotations per minute (RPM).
  • the gear box 130 is a step-up type of gear, for example, increasing the rotation speed to 5000 RPM and transmitting this rotation to the first compressor 140 and to the second compressor 150 .
  • the first low pressure compressor 140 may be of a double flow type receiving via two inputs the gas flow at an input pressure (e.g., of about 0.97 bar) and an input temperature (e.g., of about 41.5° C.), and outputting the gas flow at an output pressure (e.g., of about 3.20 bar) and an output temperature (e.g., of about 187° C.). The output gas is then cooled and input to the second compressor 150 .
  • an input pressure e.g., of about 0.97 bar
  • an input temperature e.g., of about 41.5° C.
  • an output pressure e.g., of about 3.20 bar
  • an output temperature e.g., of about 187° C.
  • the second compressor 150 may be a two-section type of compressor receiving first an input gas flow at a first input pressure (e.g., 2.85 bar) and a first input temperature (e.g., of about 40° C.) and outputting a first output flow at a first output pressure (e.g., of about 7.90 bar) and a first output temperature (e.g., of about 160° C.).
  • This first output flow is then cooled and input to the compressor 150 as a second flow at a second input pressure (e.g., 7.50 bar) and a second input temperature (e.g., of about 40° C.).
  • the compressor 150 then outputs a second output flow at a second output pressure (e.g., of about 20.8 bar) and a second output temperature (e.g., of about 166° C.).
  • the second input pressure is slightly lower than the first output pressure
  • the third input pressure is slightly lower than the second output pressure
  • the gas flow may be about 22-230000 kg/h, but flow losses of around 10% may occur during cooling.
  • the compressor has closed and shrunk fit impellers, the required compression being achieved by splitting the compression process into sub-processes performed inside the two different compressors. Reliability is sub-optimal due to the use of the two different compressors and the transition there-between. Additionally, the cost of the two compressors and the operating costs (footprint) thereof make it attractive to seek using more efficient, cheaper and reliable equipment for the compression.
  • a high pressure ratio compressor with multiple intercooling used in a turbo-compressor/generator train includes a casing with plural chambers, one or more shafts penetrating inside the chambers, and impellers mounted on the one or more shafts, inside the chambers, respectively.
  • Each chamber has a gas inlet and a gas outlet to allow gas flow to be input into and to be output from the respective chambers.
  • a gas flow is successively compressed in each of the chambers, and is cooled outside the compressor when transferring from one chamber to the next chamber among the plural chambers.
  • a turbo-compressor/generator train includes a high pressure ratio compressor with multiple intercooling.
  • the compressor has a casing with plural chambers, one or more shafts penetrating inside the chambers, and impellers mounted on the one or more shafts, inside the chambers, respectively.
  • Each chamber has a gas inlet and a gas outlet to allow gas flow to be input into and to be output from the respective chambers.
  • the gas flow is successively compressed in each of the chambers, and is cooled outside the compressor when transferring from one chamber to the next chamber among the plural chambers.
  • a method of retrofitting a conventional turbo-compressor/generator train includes (A) removing at least two compressors from the conventional turbo-compressor/generator train, and (B) adding a single high pressure ratio compressor with multiple intercooling.
  • the single compressor is configured to achieve the same compression as the removed compressors.
  • FIG. 1 is a schematic diagram of a conventional turbo-compressor/generator train
  • FIG. 2 is a schematic diagram of a turbo-compressor/generator train, according to an exemplary embodiment
  • FIG. 3 is a schematic diagram of a turbo-compressor/generator train, according to another exemplary embodiment.
  • FIG. 4 is a flowchart illustrating a method for retrofitting a conventional turbo-compressor/generator train, according to an exemplary embodiment.
  • plural impellers are mounted in the same one casing to achieve a more efficient, cheaper and reliable compressor capable of performing the duty of the two compressors in a conventional turbo-compressor/generator train.
  • FIG. 2 A schematic diagram of a turbo-compressor/generator train 200 , according to an exemplary embodiment, is illustrated in FIG. 2 .
  • the turbo-compressor/generator train 200 includes a gas turbine 210 , a generator 220 , a gear box 230 , and a single compressor 245 with multiple cooling.
  • the gas turbine 210 , the generator 220 , and the gear box 230 may be similar to the gas turbine 110 , the generator 120 , and the gear box 130 in the conventional turbo-compressor/generator train 100 .
  • the compressor 245 is a high pressure ratio compressor with multiple intercooling.
  • the ratio of the output pressure (of the gas flow output from the compressor 245 after being compressed) to the input pressure (of the gas flow input to the compressor 245 for being compressed) may be over 20.
  • Shafts 265 and 265 ′ of the compressor 245 are axially connected and may be supported by plural bearings.
  • a first bearing 260 is located outside the casing 246 of the compressor 245 , on the shaft 265 ′ at a side of the casing 245 toward the gear box 230 .
  • a second bearing 270 is also located outside the casing 246 , on the shaft 265 at the opposite side of the casing 246 relative to the side where the first bearing 260 is located.
  • the compressor 245 has three chambers 247 , 248 and 249 , each chamber having a gas inlet and a gas outlet to allow gas flow to enter and to exit the respective chamber.
  • the gas may be air.
  • the shafts 265 and 265 ′ penetrate through the chambers.
  • Impellers 257 , 258 and 259 are mounted on the shafts in chambers 247 , 248 and 249 , respectively.
  • the impellers 257 and 258 are low pressure components and may be open impeller type.
  • the impeller 259 is a high pressure component and may be of closed impeller type.
  • the low pressure components 257 and 258 may be axially stacked, while the high pressure component 259 may be either stacked type or shrunk fit onto shaft 265 ′.
  • the shafts 265 and 265 ′ and the impellers 257 , 258 and 259 are axially connected to constitute the rotor of compressor 245 .
  • the gas flow enters the first chamber 247 of the compressor 245 having a first input pressure (e.g., of about 0.97 bar) and a first input temperature (e.g., of about 41.5° C.), and is output having a first output pressure (e.g., of about 3.20 bar) higher than the first input pressure, and a first output temperature (e.g., of about 187° C.) higher than the first input temperature.
  • a first input pressure e.g., of about 0.97 bar
  • a first input temperature e.g., of about 41.5° C.
  • the output gas is then cooled (i.e., a first cooling outside the compressor) and input into the second chamber 248 of the compressor 245 having a second input pressure (e.g., 2.85 bar) and a second input temperature (e.g., of about 40° C.).
  • a second input pressure e.g., 2.85 bar
  • a second input temperature e.g., of about 40° C.
  • the gas is compressed to be output having a second output pressure (e.g., of about 7.80 bar) higher than the second input pressure, and a second output temperature (e.g., of about 160° C.) higher than the second input temperature.
  • the gas flow is then cooled again (i.e., a second cooling outside the compressor) and input into the third chamber 249 of the compressor 245 having a third input pressure (e.g., 7.50 bar) and a second input temperature (e.g., of about 40° C.).
  • a third input pressure e.g., 7.50 bar
  • a second input temperature e.g., of about 40° C.
  • the gas is compressed to be output having a third output pressure (e.g., of about 20.8 bar) higher than the third input pressure, and a third output temperature (e.g., of about 166° C.) higher than the third input temperature.
  • FIG. 3 A schematic diagram of a turbo-compressor/generator train 300 , according to another exemplary embodiment, is illustrated in FIG. 3 .
  • the turbo-compressor/generator train 300 includes a gas turbine 310 , a generator 320 , a gear box 330 , and a single compressor 345 with multiple cooling.
  • the gas turbine 310 , the generator 320 , and the gear box 330 may be similar to the gas turbine 110 , the generator 120 , and the gear box 130 in the conventional turbo-compressor/generator train 100 .
  • the compressor 345 is a high pressure ratio compressor with multiple intercooling that may achieve a ratio of the output pressure to the input pressure over 20.
  • the compressor 345 has three chambers 347 , 348 and 349 , with impellers 357 , 358 and 359 mounted on the shaft 365 therein.
  • the gas flow is compressed inside the chambers 347 , 348 and 349 in a manner similar to the manner described relative to compressor 245 .
  • the shaft 365 of compressor 345 may be supported by plural bearings.
  • a first bearing 360 is located outside the compressor 345 , at a side of the casing 346 of the compressor 345 toward the gear box 330 .
  • a second bearing 380 is located inside compressor 345 between chamber 347 and chamber 348 thereof. This arrangement of the bearings allows a higher rotation of the shaft 365 , than of shafts 265 , 265 ′, for example, up to 7000 RPM.
  • FIG. 4 is a flowchart illustrating a method 400 for retrofitting a conventional turbo-compressor/generator train, according to an exemplary embodiment.
  • the method 400 includes removing at least two compressors from the conventional turbo-compressor/generator train, at S 410 , and adding a single high pressure ratio compressor with multiple intercooling, at 5420 .
  • the single compressor is configured to achieve the same compression as the removed compressors.
  • the single compressor may have multiple chambers inside which a gas flow is compressed.
  • the single compressor may have three chambers.
  • the compressed gas flow is output from two of the chambers to be cooled outside the compressor before being directed into the next chamber.
  • the method may further include adding at least two bearings to support a shaft of the single compressor.
  • One of the added bearings may be located outside the casing of the single compressor, at a side thereof toward the gear box of the turbo-compressor/generator train.
  • a second bearing may also be located outside the casing of the single compressor, at the opposite side of the casing relative to the side where the first bearing is located.
  • a second bearing may be located inside the casing of the single compressor.
  • the second bearing may be located between chambers of the compressor.
  • the disclosed exemplary embodiments provide a turbo-compressor/generator train including a single high pressure compressor with multiple cooling and related methods. It should be understood that this description is not intended to limit the invention. On the contrary, the exemplary embodiments are intended to cover alternatives, modifications and equivalents, which are included in the spirit and scope of the invention as defined by the appended claims. Further, in the detailed description of the exemplary embodiments, numerous specific details are set forth in order to provide a comprehensive understanding of the claimed invention. However, one skilled in the art would understand that various embodiments may be practiced without such specific details.

Abstract

Turbo-compressor/generator trains including high pressure ratio compressors with multiple intercooling and related methods are provided. A high pressure ratio compressor with multiple intercooling includes a casing with plural chambers, one or more shafts penetrating inside the chambers, and impellers mounted on the one or more shafts inside the chambers, respectively. Each chamber has a gas inlet and a gas outlet to allow gas flow to be input into and to be output from the respective chamber. A gas flow is successively compressed in each of the chambers, and is cooled outside the compressor when transferring from one chamber to a next chamber among the plural chambers.

Description

    BACKGROUND
  • Embodiments of the subject matter disclosed herein generally relate to high pressure ratio compressors with multiple intercooling and related methods; more particularly, to a turbo-compressor/generator train using a high pressure compressor with multiple intercooling instead of plural compressors.
  • One type of turbo-machinery is a centrifugal compressor. Centrifugal compressors are usually designed in families intended to cover a specific flow range and use. In order to achieve a desired compression ratio, a centrifugal compressor may be arranged to perform compression one after another. For example, two centrifugal compressors are typically arranged in a turbo-compressor/generator train 100 as illustrated in FIG. 1. Such turbo-compressor/generator trains may be used for blast furnaces in the steel industry, natural gas liquefaction, gas reinjection and other oil and gas services.
  • Five machines are mechanically coupled in the turbo-compressor/generator train 100: a gas turbine 110, a generator 120, a gear box 130, a first low pressure compressor 140, and a second compressor 150. This type of arrangement is sometimes called a “single-shaft” configuration.
  • The generator 120 may have a rotation speed of 3000 rotations per minute (RPM). The gear box 130 is a step-up type of gear, for example, increasing the rotation speed to 5000 RPM and transmitting this rotation to the first compressor 140 and to the second compressor 150.
  • The first low pressure compressor 140 may be of a double flow type receiving via two inputs the gas flow at an input pressure (e.g., of about 0.97 bar) and an input temperature (e.g., of about 41.5° C.), and outputting the gas flow at an output pressure (e.g., of about 3.20 bar) and an output temperature (e.g., of about 187° C.). The output gas is then cooled and input to the second compressor 150.
  • The second compressor 150 may be a two-section type of compressor receiving first an input gas flow at a first input pressure (e.g., 2.85 bar) and a first input temperature (e.g., of about 40° C.) and outputting a first output flow at a first output pressure (e.g., of about 7.90 bar) and a first output temperature (e.g., of about 160° C.). This first output flow is then cooled and input to the compressor 150 as a second flow at a second input pressure (e.g., 7.50 bar) and a second input temperature (e.g., of about 40° C.). The compressor 150 then outputs a second output flow at a second output pressure (e.g., of about 20.8 bar) and a second output temperature (e.g., of about 166° C.).
  • Note that the second input pressure is slightly lower than the first output pressure, and the third input pressure is slightly lower than the second output pressure. Also, the gas flow may be about 22-230000 kg/h, but flow losses of around 10% may occur during cooling.
  • In the conventional turbo-compressor/generator train, the compressor has closed and shrunk fit impellers, the required compression being achieved by splitting the compression process into sub-processes performed inside the two different compressors. Reliability is sub-optimal due to the use of the two different compressors and the transition there-between. Additionally, the cost of the two compressors and the operating costs (footprint) thereof make it attractive to seek using more efficient, cheaper and reliable equipment for the compression.
  • Accordingly, it would be desirable to provide a high pressure compressor with multiple intercooling and related methods that avoid the afore-described problems and drawbacks.
  • BRIEF DESCRIPTION OF THE INVENTION
  • The use of a high pressure air compressor with two levels of intercooling instead of two compressors in a turbo-compressor/generator train allows removal of one large casing, leading to a benefit in size, cost, overall reliability and footprint.
  • According to one exemplary embodiment, a high pressure ratio compressor with multiple intercooling used in a turbo-compressor/generator train includes a casing with plural chambers, one or more shafts penetrating inside the chambers, and impellers mounted on the one or more shafts, inside the chambers, respectively. Each chamber has a gas inlet and a gas outlet to allow gas flow to be input into and to be output from the respective chambers. A gas flow is successively compressed in each of the chambers, and is cooled outside the compressor when transferring from one chamber to the next chamber among the plural chambers.
  • According to another embodiment, a turbo-compressor/generator train includes a high pressure ratio compressor with multiple intercooling. The compressor has a casing with plural chambers, one or more shafts penetrating inside the chambers, and impellers mounted on the one or more shafts, inside the chambers, respectively. Each chamber has a gas inlet and a gas outlet to allow gas flow to be input into and to be output from the respective chambers. The gas flow is successively compressed in each of the chambers, and is cooled outside the compressor when transferring from one chamber to the next chamber among the plural chambers.
  • According to another exemplary embodiment, a method of retrofitting a conventional turbo-compressor/generator train includes (A) removing at least two compressors from the conventional turbo-compressor/generator train, and (B) adding a single high pressure ratio compressor with multiple intercooling. The single compressor is configured to achieve the same compression as the removed compressors.
  • BRIEF DESCRIPTION OF THE DRAWINGS
  • The accompanying drawings, which are incorporated in and constitute a part of the specification, illustrate one or more embodiments and, together with the description, explain these embodiments. In the drawings:
  • FIG. 1 is a schematic diagram of a conventional turbo-compressor/generator train;
  • FIG. 2 is a schematic diagram of a turbo-compressor/generator train, according to an exemplary embodiment;
  • FIG. 3 is a schematic diagram of a turbo-compressor/generator train, according to another exemplary embodiment; and
  • FIG. 4 is a flowchart illustrating a method for retrofitting a conventional turbo-compressor/generator train, according to an exemplary embodiment.
  • DETAILED DESCRIPTION OF THE INVENTION
  • The following description of the exemplary embodiments refers to the accompanying drawings. The same reference numbers in different drawings identify the same or similar elements. The following detailed description does not limit the invention. Instead, the scope of the invention is defined by the appended claims. The following embodiments are discussed, for simplicity, with regard to the terminology and structure of a turbo-compressor/generator train. However, the embodiments to be discussed next are not limited to these systems, but may be applied to other systems in which plural compressors are used.
  • Reference throughout the specification to “one embodiment” or “an embodiment” means that a particular feature, structure or characteristic described in connection with an embodiment is included in at least one embodiment of the subject matter disclosed. Thus, the appearance of the phrases “in one embodiment” or “in an embodiment” in various places throughout the specification is not necessarily referring to the same embodiment. Further, the particular features, structures or characteristics may be combined in any suitable manner in one or more embodiments.
  • In some embodiments, plural impellers are mounted in the same one casing to achieve a more efficient, cheaper and reliable compressor capable of performing the duty of the two compressors in a conventional turbo-compressor/generator train.
  • A schematic diagram of a turbo-compressor/generator train 200, according to an exemplary embodiment, is illustrated in FIG. 2. The turbo-compressor/generator train 200 includes a gas turbine 210, a generator 220, a gear box 230, and a single compressor 245 with multiple cooling. The gas turbine 210, the generator 220, and the gear box 230 may be similar to the gas turbine 110, the generator 120, and the gear box 130 in the conventional turbo-compressor/generator train 100.
  • The compressor 245 is a high pressure ratio compressor with multiple intercooling. The ratio of the output pressure (of the gas flow output from the compressor 245 after being compressed) to the input pressure (of the gas flow input to the compressor 245 for being compressed) may be over 20. Shafts 265 and 265′ of the compressor 245 are axially connected and may be supported by plural bearings. In FIG. 2, a first bearing 260 is located outside the casing 246 of the compressor 245, on the shaft 265′ at a side of the casing 245 toward the gear box 230. A second bearing 270 is also located outside the casing 246, on the shaft 265 at the opposite side of the casing 246 relative to the side where the first bearing 260 is located.
  • The compressor 245 has three chambers 247, 248 and 249, each chamber having a gas inlet and a gas outlet to allow gas flow to enter and to exit the respective chamber. The gas may be air. The shafts 265 and 265′ penetrate through the chambers. Impellers 257, 258 and 259 are mounted on the shafts in chambers 247, 248 and 249, respectively. The impellers 257 and 258 are low pressure components and may be open impeller type. The impeller 259 is a high pressure component and may be of closed impeller type. The low pressure components 257 and 258 may be axially stacked, while the high pressure component 259 may be either stacked type or shrunk fit onto shaft 265′. The shafts 265 and 265′ and the impellers 257, 258 and 259 are axially connected to constitute the rotor of compressor 245.
  • The gas flow enters the first chamber 247 of the compressor 245 having a first input pressure (e.g., of about 0.97 bar) and a first input temperature (e.g., of about 41.5° C.), and is output having a first output pressure (e.g., of about 3.20 bar) higher than the first input pressure, and a first output temperature (e.g., of about 187° C.) higher than the first input temperature.
  • The output gas is then cooled (i.e., a first cooling outside the compressor) and input into the second chamber 248 of the compressor 245 having a second input pressure (e.g., 2.85 bar) and a second input temperature (e.g., of about 40° C.). Inside the second chamber 248, the gas is compressed to be output having a second output pressure (e.g., of about 7.80 bar) higher than the second input pressure, and a second output temperature (e.g., of about 160° C.) higher than the second input temperature.
  • The gas flow is then cooled again (i.e., a second cooling outside the compressor) and input into the third chamber 249 of the compressor 245 having a third input pressure (e.g., 7.50 bar) and a second input temperature (e.g., of about 40° C.). Inside the third chamber 249, the gas is compressed to be output having a third output pressure (e.g., of about 20.8 bar) higher than the third input pressure, and a third output temperature (e.g., of about 166° C.) higher than the third input temperature.
  • A schematic diagram of a turbo-compressor/generator train 300, according to another exemplary embodiment, is illustrated in FIG. 3. The turbo-compressor/generator train 300 includes a gas turbine 310, a generator 320, a gear box 330, and a single compressor 345 with multiple cooling. The gas turbine 310, the generator 320, and the gear box 330 may be similar to the gas turbine 110, the generator 120, and the gear box 130 in the conventional turbo-compressor/generator train 100.
  • Similar to compressor 245, the compressor 345 is a high pressure ratio compressor with multiple intercooling that may achieve a ratio of the output pressure to the input pressure over 20. The compressor 345 has three chambers 347, 348 and 349, with impellers 357, 358 and 359 mounted on the shaft 365 therein. The gas flow is compressed inside the chambers 347, 348 and 349 in a manner similar to the manner described relative to compressor 245.
  • The shaft 365 of compressor 345 may be supported by plural bearings. A first bearing 360 is located outside the compressor 345, at a side of the casing 346 of the compressor 345 toward the gear box 330. Different from compressor 245, a second bearing 380 is located inside compressor 345 between chamber 347 and chamber 348 thereof. This arrangement of the bearings allows a higher rotation of the shaft 365, than of shafts 265, 265′, for example, up to 7000 RPM.
  • Conventional turbo-compressor/generator trains may be retrofitted by replacing the two compressors with a single high pressure ratio compressor with multiple intercooling. FIG. 4 is a flowchart illustrating a method 400 for retrofitting a conventional turbo-compressor/generator train, according to an exemplary embodiment. The method 400 includes removing at least two compressors from the conventional turbo-compressor/generator train, at S410, and adding a single high pressure ratio compressor with multiple intercooling, at 5420. The single compressor is configured to achieve the same compression as the removed compressors.
  • The single compressor may have multiple chambers inside which a gas flow is compressed. For example, the single compressor may have three chambers. The compressed gas flow is output from two of the chambers to be cooled outside the compressor before being directed into the next chamber.
  • The method may further include adding at least two bearings to support a shaft of the single compressor. One of the added bearings may be located outside the casing of the single compressor, at a side thereof toward the gear box of the turbo-compressor/generator train. In one embodiment a second bearing may also be located outside the casing of the single compressor, at the opposite side of the casing relative to the side where the first bearing is located. In another embodiment, a second bearing may be located inside the casing of the single compressor. For example, the second bearing may be located between chambers of the compressor.
  • The disclosed exemplary embodiments provide a turbo-compressor/generator train including a single high pressure compressor with multiple cooling and related methods. It should be understood that this description is not intended to limit the invention. On the contrary, the exemplary embodiments are intended to cover alternatives, modifications and equivalents, which are included in the spirit and scope of the invention as defined by the appended claims. Further, in the detailed description of the exemplary embodiments, numerous specific details are set forth in order to provide a comprehensive understanding of the claimed invention. However, one skilled in the art would understand that various embodiments may be practiced without such specific details.
  • Although the features and elements of the present exemplary embodiments are described in the embodiments in particular combinations, each feature or element can be used alone without the other features and elements of the embodiments or in various combinations with or without other features and elements disclosed herein.
  • This written description uses examples of the subject matter disclosed to enable any person skilled in the art to practice the same, including making and using any devices or systems and performing any incorporated methods. The patentable scope of the subject matter is defined by the claims, and may include other examples that occur to those skilled in the art. Such other examples are intended to be within the scope of the claims.

Claims (20)

What is claimed is:
1. A high pressure ratio compressor with multiple intercooling used in a turbo-compressor/generator train, the compressor comprising:
a casing with plural chambers, each chamber comprising a gas inlet and a gas outlet to allow gas flow to be input into and to be output from the respective chamber;
one or more shafts penetrating inside the chambers; and
impellers mounted on the one or more shafts, inside the chambers, respectively,
wherein a gas flow is successively compressed in each of the chambers, and is cooled outside the casing when transferring from one chamber to a next chamber among the plural chambers.
2. The compressor of claim 1, wherein the compressor is configured to achieve a compression ratio over 20, for a gas flow around 220000 kg/h.
3. The compressor of claim 1, further comprising plural bearings supporting the shaft, wherein one of the plural bearings is located on the shaft outside the casing, at a side of the casing towards a gear box of the turbo-compressor/generator train.
4. The compressor of claim 3, wherein one of the plural bearings is located on the shaft outside the casing, at an opposite side of the casing relative to the side of the casing towards the gear box.
5. The compressor of claim 3, wherein one of the plural bearings is located on the shaft inside the casing, near a wall separating chambers of the compressor.
6. The compressor of claim 5, wherein the chambers are arranged in an order corresponding to an output pressure of the gas flow, the another one of the plural bearings being located near the wall separating lower pressure chambers of the compressor, and the one of the plural bearings being located near a chamber corresponding to the highest output pressure.
7. The compressor of claim 1, wherein the chambers comprise three chambers, and pressure of the gas flow output from one chamber drops about 10% while being cooled outside the casing before being input into the next chamber.
8. The compressor of claim 1, wherein the compressor is configured to meet at least one of the following conditions:
temperatures of the gas flow input in each of the chambers is around 40° C.; a ratio of pressure of the gas flow output from each chamber to pressure of the gas flow input in the respective chamber is between 2.5 and 3.5;
an input pressure of the gas flow input in a first chamber of the compressor is about 1 bar;
an output pressure of the gas flow output from the compressor is about 20.8 bar; and
a rotation speed of the one or more shafts is between 5000-7000 RPM.
9. (canceled)
10. A turbo-compressor/generator train, comprising:
a high pressure ratio compressor with multiple intercooling, compressor comprising:
a casing with plural chambers, each chamber comprising a gas inlet and a gas outlet to allow gas flow be input into and to be output from the respective chamber;
one or more shafts penetrating inside the chambers; and
impellers mounted on the one or more shafts inside the chambers, respectively,
wherein a gas flow is successively compressed in each of the chambers, and is cooled outside the casing when transferring from one chamber to a next chamber among the plural chambers.
11. A method of retrofitting a conventional turbo-compressor/generator train, the method comprising:
removing at least two compressors from the conventional turbo-compressor/generator train; and
adding a single high pressure ratio compressor with multiple intercooling,
wherein the single compressor is configured to achieve the same compression as the removed compressors.
12. The compressor of claim 3, wherein the compressor is configured to achieve a compression ratio over 20, for a gas flow around 220000 kg/h.
13. The compressor of claim 4, wherein the compressor is configured to achieve a compression ratio over 20, for a gas flow around 220000 kg/h.
14. The compressor of claim 5, wherein the compressor is configured to achieve a compression ratio over 20, for a gas flow around 220000 kg/h.
15. The compressor of claim 7, wherein the compressor is configured to achieve a compression ratio over 20, for a gas flow around 220000 kg/h.
16. The compressor of claim 8, wherein the compressor is configured to achieve a compression ratio over 20, for a gas flow around 220000 kg/h.
17. The compressor of claim 3, wherein the chambers comprise three chambers, and pressure of the gas flow output from one chamber drops about 10% while being cooled outside the casing before being input into the next chamber.
18. The compressor of claim 12, wherein the chambers comprise three chambers, and pressure of the gas flow output from one chamber drops about 10% while being cooled outside the casing before being input into the next chamber.
19. The compressor of claim 18, wherein the compressor is configured to meet at least one of the following conditions:
temperatures of the gas flow input in each of the chambers is around 40° C.; a ratio of pressure of the gas flow output from each chamber to pressure of the gas flow input in the respective chamber is between 2.5 and 3.5;
an input pressure of the gas flow input in a first chamber of the compressor is about 1 bar;
an output pressure of the gas flow output from the compressor is about 20.8 bar; and
a rotation speed of the one or more shafts is between 5000-7000 RPM.
20. The compressor of claim 3, wherein the compressor is configured to meet at least one of the following conditions:
temperatures of the gas flow input in each of the chambers is around 40° C.; a ratio of pressure of the gas flow output from each chamber to pressure of the gas flow input in the respective chamber is between 2.5 and 3.5;
an input pressure of the gas flow input in a first chamber of the compressor is about 1 bar;
an output pressure of the gas flow output from the compressor is about 20.8 bar; and
a rotation speed of the one or more shafts is between 5000-7000 RPM.
US14/405,855 2012-06-06 2013-05-31 High pressure ratio compressors with multiple intercooling and related methods Abandoned US20150152884A1 (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2018115660A1 (en) 2016-12-22 2018-06-28 Engie Device and method for liquefying a natural gas and ship comprising such a device
IT201700007473A1 (en) * 2017-01-24 2018-07-24 Nuovo Pignone Tecnologie Srl COMPRESSION TRAIN WITH A CENTRIFUGAL COMPRESSOR AND LNG PLANT
US20180238236A1 (en) * 2015-07-24 2018-08-23 Nuovo Pignone Technologie Srl Charge gas compression train for ethylene
US20180347571A1 (en) * 2015-12-04 2018-12-06 Mitsubishi Heavy Industries Compressor Corporation Centrifugal compressor

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ITCO20130069A1 (en) 2013-12-18 2015-06-19 Nuovo Pignone Srl MULTI-STAGE CENTRIFUGAL COMPRESSOR
ITUB20152489A1 (en) * 2015-07-24 2017-01-24 Nuovo Pignone Tecnologie Srl COMPRESSION TRAIN WITH AN AXIAL COMPRESSOR AND LNG SYSTEM WITH AN AXIAL COMPRESSOR
EP3325811A1 (en) * 2015-07-24 2018-05-30 Nuovo Pignone Tecnologie SrL Lng plant including an axial compressor and a centrifugal compressor
ITUB20152501A1 (en) * 2015-07-24 2017-01-24 Nuovo Pignone Tecnologie Srl COMPRESSION TRAIN WITH A CENTRIFUGAL COMPRESSOR AND LNG SYSTEM WITH A CENTRIFUGAL COMPRESSOR
ITUA20164168A1 (en) * 2016-06-07 2017-12-07 Nuovo Pignone Tecnologie Srl COMPRESSION TRAIN WITH TWO CENTRIFUGAL COMPRESSORS AND LNG PLANT WITH TWO CENTRIFUGAL COMPRESSORS
IT201800011099A1 (en) * 2018-12-14 2020-06-14 Nuovo Pignone Tecnologie Srl PROPANE DE-HYDROGENATION SYSTEM WITH A SINGLE BOX REACTOR EFFLUENT COMPRESSOR AND METHOD

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1050419A (en) * 1912-03-21 1913-01-14 Ingersoll Rand Co Centrifugal compressor.
US3717418A (en) * 1970-06-08 1973-02-20 Carrier Corp Compressor barrel assembly
US5062766A (en) * 1988-09-14 1991-11-05 Hitachi, Ltd. Turbo compressor
US5735672A (en) * 1996-09-16 1998-04-07 Delaware Capital Formation, Inc. Centrifugal compressor impeller
US20090056303A1 (en) * 2006-06-26 2009-03-05 Hidefumi Araki Cooling apparatus, gas turbine system using cooling apparatus, heat pump system using cooling system, cooling method, and method for operating cooling apparatus

Family Cites Families (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR1293655A (en) * 1961-04-07 1962-05-18 Rateau Soc Improvements to multi-stage compressors with intermediate refrigeration
DE1428047B2 (en) * 1962-07-13 1970-11-12 Badische Anilin- & Soda-Fabrik AG, 67OO Ludwigshafen Control arrangement for the condensate-free operation of multi-stage turbo compressors cooled in each intermediate stage
GB1314147A (en) * 1971-07-22 1973-04-18 Carrier Corp High pressure centrifugal compressor
SU844824A1 (en) * 1979-10-09 1981-07-07 Всесоюзное Научно-Производственноеобъединение "Союзтурбогаз" Natural gas supercharger
DE3729486C1 (en) * 1987-09-03 1988-12-15 Gutehoffnungshuette Man Compressor unit
US20020050345A1 (en) * 2000-10-31 2002-05-02 Haruo Miura Heat exchanger for air compressor
TWI325946B (en) * 2004-01-30 2010-06-11 Sanyo Electric Co Heating/cooling system
EP1696135A1 (en) * 2005-01-27 2006-08-30 Siemens Aktiengesellschaft Intercooled turbocompressor
EP1999374A1 (en) * 2006-03-24 2008-12-10 Siemens Aktiengesellschaft Compressor unit
DE102009038786A1 (en) * 2009-08-25 2011-05-05 Siemens Aktiengesellschaft compressor
KR101603218B1 (en) * 2010-03-16 2016-03-15 한화테크윈 주식회사 Turbine system

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1050419A (en) * 1912-03-21 1913-01-14 Ingersoll Rand Co Centrifugal compressor.
US3717418A (en) * 1970-06-08 1973-02-20 Carrier Corp Compressor barrel assembly
US5062766A (en) * 1988-09-14 1991-11-05 Hitachi, Ltd. Turbo compressor
US5735672A (en) * 1996-09-16 1998-04-07 Delaware Capital Formation, Inc. Centrifugal compressor impeller
US20090056303A1 (en) * 2006-06-26 2009-03-05 Hidefumi Araki Cooling apparatus, gas turbine system using cooling apparatus, heat pump system using cooling system, cooling method, and method for operating cooling apparatus

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20180238236A1 (en) * 2015-07-24 2018-08-23 Nuovo Pignone Technologie Srl Charge gas compression train for ethylene
US10724439B2 (en) * 2015-07-24 2020-07-28 Nuovo Pignone Srl Charge gas compression train for ethylene
US20180347571A1 (en) * 2015-12-04 2018-12-06 Mitsubishi Heavy Industries Compressor Corporation Centrifugal compressor
US10670025B2 (en) * 2015-12-04 2020-06-02 Mitsubishi Heavy Industries Compressor Corporation Centrifugal compressor
WO2018115660A1 (en) 2016-12-22 2018-06-28 Engie Device and method for liquefying a natural gas and ship comprising such a device
FR3061278A1 (en) * 2016-12-22 2018-06-29 Engie DEVICE AND METHOD FOR LIQUEFACTING A NATURAL GAS AND SHIP COMPRISING SUCH A DEVICE
CN110573814A (en) * 2016-12-22 2019-12-13 前苏伊士环能集团 apparatus and method for liquefying natural gas and ship comprising the same
IT201700007473A1 (en) * 2017-01-24 2018-07-24 Nuovo Pignone Tecnologie Srl COMPRESSION TRAIN WITH A CENTRIFUGAL COMPRESSOR AND LNG PLANT
EP3351882A1 (en) * 2017-01-24 2018-07-25 Nuovo Pignone Tecnologie SrL Compression train including one centrifugal compressor and lng plant
US20180209728A1 (en) * 2017-01-24 2018-07-26 Nuovo Pignone Tecnologie - S.R.L. Compression train including one centrifugal compressor and lng plant
US10809000B2 (en) * 2017-01-24 2020-10-20 Nuovo Pignone Tecnologie Srl Compression train including one centrifugal compressor and LNG plant

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