US20150377244A1 - System and method for compressing air - Google Patents

System and method for compressing air Download PDF

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Publication number
US20150377244A1
US20150377244A1 US14/843,430 US201514843430A US2015377244A1 US 20150377244 A1 US20150377244 A1 US 20150377244A1 US 201514843430 A US201514843430 A US 201514843430A US 2015377244 A1 US2015377244 A1 US 2015377244A1
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United States
Prior art keywords
speed
compression
motor
air
inlet guide
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US14/843,430
Inventor
Michael J. Stanko
John H. Royal
Ahmed F. Abdelwahab
Carl L. Schwarz
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Praxair Technology Inc
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Praxair Technology Inc
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Priority to US14/843,430 priority Critical patent/US20150377244A1/en
Assigned to PRAXAIR TECHNOLOGY, INC. reassignment PRAXAIR TECHNOLOGY, INC. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: ABDELWAHAB, AHMED F., ROYAL, JOHN H., SCHWARZ, CARL L., STANKO, MICHAEL J.
Publication of US20150377244A1 publication Critical patent/US20150377244A1/en
Abandoned legal-status Critical Current

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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
    • F04D27/00Control, e.g. regulation, of pumps, pumping installations or pumping systems specially adapted for elastic fluids
    • F04D27/004Control, e.g. regulation, of pumps, pumping installations or pumping systems specially adapted for elastic fluids by varying driving speed
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04BPOSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
    • F04B37/00Pumps having pertinent characteristics not provided for in, or of interest apart from, groups F04B25/00 - F04B35/00
    • F04B37/06Pumps having pertinent characteristics not provided for in, or of interest apart from, groups F04B25/00 - F04B35/00 for evacuating by thermal means
    • F04B37/08Pumps having pertinent characteristics not provided for in, or of interest apart from, groups F04B25/00 - F04B35/00 for evacuating by thermal means by condensing or freezing, e.g. cryogenic pumps
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04BPOSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
    • F04B49/00Control, e.g. of pump delivery, or pump pressure of, or safety measures for, machines, pumps, or pumping installations, not otherwise provided for, or of interest apart from, groups F04B1/00 - F04B47/00
    • F04B49/06Control using electricity
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04BPOSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
    • F04B49/00Control, e.g. of pump delivery, or pump pressure of, or safety measures for, machines, pumps, or pumping installations, not otherwise provided for, or of interest apart from, groups F04B1/00 - F04B47/00
    • F04B49/10Other safety measures
    • F04B49/103Responsive to speed
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04BPOSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
    • F04B49/00Control, e.g. of pump delivery, or pump pressure of, or safety measures for, machines, pumps, or pumping installations, not otherwise provided for, or of interest apart from, groups F04B1/00 - F04B47/00
    • F04B49/20Control, e.g. of pump delivery, or pump pressure of, or safety measures for, machines, pumps, or pumping installations, not otherwise provided for, or of interest apart from, groups F04B1/00 - F04B47/00 by changing the driving speed
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04CROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT PUMPS
    • F04C28/00Control of, monitoring of, or safety arrangements for, pumps or pumping installations specially adapted for elastic fluids
    • F04C28/10Control of, monitoring of, or safety arrangements for, pumps or pumping installations specially adapted for elastic fluids characterised by changing the positions of the inlet or outlet openings with respect to the working chamber
    • F04C28/14Control of, monitoring of, or safety arrangements for, pumps or pumping installations specially adapted for elastic fluids characterised by changing the positions of the inlet or outlet openings with respect to the working chamber using rotating valves
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
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    • 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
    • F04D25/00Pumping installations or systems
    • F04D25/02Units comprising pumps and their driving means
    • F04D25/06Units comprising pumps and their driving means the pump being electrically driven
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04DNON-POSITIVE-DISPLACEMENT PUMPS
    • F04D27/00Control, e.g. regulation, of pumps, pumping installations or pumping systems specially adapted for elastic fluids
    • F04D27/02Surge control
    • F04D27/0246Surge control by varying geometry within the pumps, e.g. by adjusting vanes
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04DNON-POSITIVE-DISPLACEMENT PUMPS
    • F04D27/00Control, e.g. regulation, of pumps, pumping installations or pumping systems specially adapted for elastic fluids
    • F04D27/02Surge control
    • F04D27/0261Surge control by varying driving speed
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04DNON-POSITIVE-DISPLACEMENT PUMPS
    • F04D27/00Control, e.g. regulation, of pumps, pumping installations or pumping systems specially adapted for elastic fluids
    • F04D27/02Surge control
    • F04D27/0269Surge control by changing flow path between different stages or between a plurality of compressors; load distribution between compressors
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04DNON-POSITIVE-DISPLACEMENT PUMPS
    • F04D27/00Control, e.g. regulation, of pumps, pumping installations or pumping systems specially adapted for elastic fluids
    • F04D27/02Surge control
    • F04D27/0284Conjoint control of two or more different functions
    • 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
    • F04D29/05Shafts or bearings, or assemblies thereof, specially adapted for elastic fluid pumps
    • F04D29/053Shafts
    • 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
    • F04D29/26Rotors specially for elastic fluids
    • F04D29/28Rotors specially for elastic fluids for centrifugal or helico-centrifugal pumps for radial-flow or helico-centrifugal pumps
    • F04D29/284Rotors specially for elastic fluids for centrifugal or helico-centrifugal pumps for radial-flow or helico-centrifugal pumps for compressors
    • F04D29/286Rotors specially for elastic fluids for centrifugal or helico-centrifugal pumps for radial-flow or helico-centrifugal pumps for compressors multi-stage rotors
    • 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
    • F04D29/40Casings; Connections of working fluid
    • F04D29/42Casings; Connections of working fluid for radial or helico-centrifugal pumps
    • F04D29/44Fluid-guiding means, e.g. diffusers
    • F04D29/46Fluid-guiding means, e.g. diffusers adjustable
    • F04D29/462Fluid-guiding means, e.g. diffusers adjustable especially adapted for elastic fluid 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
    • F04D29/40Casings; Connections of working fluid
    • F04D29/42Casings; Connections of working fluid for radial or helico-centrifugal pumps
    • F04D29/44Fluid-guiding means, e.g. diffusers
    • F04D29/46Fluid-guiding means, e.g. diffusers adjustable
    • F04D29/462Fluid-guiding means, e.g. diffusers adjustable especially adapted for elastic fluid pumps
    • F04D29/464Fluid-guiding means, e.g. diffusers adjustable especially adapted for elastic fluid pumps adjusting flow cross-section, otherwise than by using adjustable stator blades
    • 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
    • F04D29/66Combating cavitation, whirls, noise, vibration or the like; Balancing
    • F04D29/661Combating cavitation, whirls, noise, vibration or the like; Balancing especially adapted for elastic fluid pumps
    • F04D29/668Combating cavitation, whirls, noise, vibration or the like; Balancing especially adapted for elastic fluid pumps damping or preventing mechanical vibrations
    • 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
    • F25J3/00Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/04Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
    • F25J3/04006Providing pressurised feed air or process streams within or from the air fractionation unit
    • F25J3/04012Providing pressurised feed air or process streams within or from the air fractionation unit by compression of warm gaseous streams; details of intake or interstage cooling
    • F25J3/04018Providing pressurised feed air or process streams within or from the air fractionation unit by compression of warm gaseous streams; details of intake or interstage cooling of main feed air
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    • 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
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    • F25J3/02Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/04Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
    • F25J3/04006Providing pressurised feed air or process streams within or from the air fractionation unit
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    • F25J3/04024Providing pressurised feed air or process streams within or from the air fractionation unit by compression of warm gaseous streams; details of intake or interstage cooling of purified feed air, so-called boosted air
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    • 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
    • F25J3/00Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/04Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
    • F25J3/04006Providing pressurised feed air or process streams within or from the air fractionation unit
    • F25J3/04078Providing pressurised feed air or process streams within or from the air fractionation unit providing pressurized products by liquid compression and vaporisation with cold recovery, i.e. so-called internal compression
    • F25J3/0409Providing pressurised feed air or process streams within or from the air fractionation unit providing pressurized products by liquid compression and vaporisation with cold recovery, i.e. so-called internal compression of oxygen
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    • 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
    • F25J3/00Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/04Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
    • F25J3/04006Providing pressurised feed air or process streams within or from the air fractionation unit
    • F25J3/04109Arrangements of compressors and /or their drivers
    • F25J3/04115Arrangements of compressors and /or their drivers characterised by the type of prime driver, e.g. hot gas expander
    • F25J3/04133Electrical motor as the prime mechanical driver
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    • 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
    • F25J3/00Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/04Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
    • F25J3/04248Generation of cold for compensating heat leaks or liquid production, e.g. by Joule-Thompson expansion
    • F25J3/04284Generation of cold for compensating heat leaks or liquid production, e.g. by Joule-Thompson expansion using internal refrigeration by open-loop gas work expansion, e.g. of intermediate or oxygen enriched (waste-)streams
    • F25J3/0429Generation of cold for compensating heat leaks or liquid production, e.g. by Joule-Thompson expansion using internal refrigeration by open-loop gas work expansion, e.g. of intermediate or oxygen enriched (waste-)streams of feed air, e.g. used as waste or product air or expanded into an auxiliary column
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
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    • 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
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    • F25J3/02Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/04Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
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    • F25J3/04284Generation of cold for compensating heat leaks or liquid production, e.g. by Joule-Thompson expansion using internal refrigeration by open-loop gas work expansion, e.g. of intermediate or oxygen enriched (waste-)streams
    • F25J3/0429Generation of cold for compensating heat leaks or liquid production, e.g. by Joule-Thompson expansion using internal refrigeration by open-loop gas work expansion, e.g. of intermediate or oxygen enriched (waste-)streams of feed air, e.g. used as waste or product air or expanded into an auxiliary column
    • F25J3/04296Claude expansion, i.e. expanded into the main or high pressure column
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    • F25J3/04284Generation of cold for compensating heat leaks or liquid production, e.g. by Joule-Thompson expansion using internal refrigeration by open-loop gas work expansion, e.g. of intermediate or oxygen enriched (waste-)streams
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    • F25J3/04303Lachmann expansion, i.e. expanded into oxygen producing or low pressure column
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    • F25J3/04412Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air using a dual pressure main column system in a classical double column flowsheet, i.e. with thermal coupling by a main reboiler-condenser in the bottom of low pressure respectively top of high pressure column
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    • F25J3/04648Recovering noble gases from air argon
    • F25J3/04654Producing crude argon in a crude argon column
    • F25J3/04666Producing crude argon in a crude argon column as a parallel working rectification column of the low pressure column in a dual pressure main column system
    • F25J3/04672Producing crude argon in a crude argon column as a parallel working rectification column of the low pressure column in a dual pressure main column system having a top condenser
    • F25J3/04678Producing crude argon in a crude argon column as a parallel working rectification column of the low pressure column in a dual pressure main column system having a top condenser cooled by oxygen enriched liquid from high pressure column bottoms
    • 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
    • F25J3/00Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/04Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
    • F25J3/04763Start-up or control of the process; Details of the apparatus used
    • F25J3/04769Operation, control and regulation of the process; Instrumentation within the process
    • F25J3/04781Pressure changing devices, e.g. for compression, expansion, liquid pumping
    • 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
    • F25J3/00Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/04Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
    • F25J3/04763Start-up or control of the process; Details of the apparatus used
    • F25J3/04866Construction and layout of air fractionation equipments, e.g. valves, machines
    • F25J3/04872Vertical layout of cold equipments within in the cold box, e.g. columns, heat exchangers etc.
    • F25J3/04884Arrangement of reboiler-condensers
    • 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
    • F25J3/00Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/04Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
    • F25J3/04763Start-up or control of the process; Details of the apparatus used
    • F25J3/04866Construction and layout of air fractionation equipments, e.g. valves, machines
    • F25J3/04951Arrangements of multiple air fractionation units or multiple equipments fulfilling the same process step, e.g. multiple trains in a network
    • F25J3/04957Arrangements of multiple air fractionation units or multiple equipments fulfilling the same process step, e.g. multiple trains in a network and inter-connecting equipments upstream of the fractionation unit (s), i.e. at the "front-end"
    • 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
    • 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
    • F25J2230/24Multiple compressors or compressor stages in parallel
    • 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
    • F25J2230/40Processes or apparatus involving steps for increasing the pressure of gaseous process streams the fluid being air
    • 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
    • F25J2250/00Details related to the use of reboiler-condensers
    • F25J2250/02Bath type boiler-condenser using thermo-siphon effect, e.g. with natural or forced circulation or pool boiling, i.e. core-in-kettle heat exchanger
    • 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02BCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/70Efficient control or regulation technologies, e.g. for control of refrigerant flow, motor or heating

Definitions

  • the present invention relates to a method and apparatus for producing a compressed gas and for controlling the flow rate of the compressed gas in which a compressor is directly coupled to an electric motor and a restricted speed zone exists where vibrational modes can damage the electric motor and/or the compressor. More particularly, the present invention relates to such a method and apparatus in which a desired flow rate is obtained by controlling the speed of the electric motor when such flow rate can be obtained by a speed that is not within the restricted speed zone and through inlet guide vane manipulation when such flow rate would otherwise be obtained by a speed within the restricted speed zone.
  • Gases are typically compressed in compressors that are driven by electric motors.
  • the compressors can be connected so that the gas is compressed in stages from ambient to a high delivery pressure. Interstage cooling is employed to remove the heat of compressor between stages.
  • a common compressor design that is utilized is a centrifugal compressor. In a centrifugal compressor, the gas to be compressed enters an inlet and is compressed by action of an impeller that is rotated by the electric motor. The gas then passes through a diffuser and is discharged from a volute of spiral-like configuration.
  • the gas flow rate through a compression system can be controlled by an arrangement of inlet guide vanes that can be set from an open position to increasing more closed positions to impart a swirl into the incoming gas and thereby decrease the gas flow rate.
  • inlet guide vanes that can be set from an open position to increasing more closed positions to impart a swirl into the incoming gas and thereby decrease the gas flow rate.
  • high speed motors have become available that can be directly coupled to a compressor. Such motors also have a speed control that allows the speed of the compressor to be accurately controlled. This control of speed allows the flow rate of the gas to also be controlled in a more thermodynamically efficient manner than with the use of inlet guide vanes.
  • An example of such a motor are permanent magnet motors having a variable frequency drive to control the speed.
  • Such motors can be directly connected to the compressors or each of the compressors in a compression system.
  • the present invention provides a method and apparatus for compressing the gas in which desired flow rates of the gas can be safely obtained over the entire operational range of the motor while the overall compressors thermodynamic efficiency is maximized.
  • the present invention may be characterized as a compression train system for an air separation unit comprising: (a) at least one variable speed motor having at least one shaft; (b) at least one air compressor having at least one initial compression stage and adapted to receive and compress a flow of ambient pressure air and to be driven by the at least one shaft of the variable speed motor; and (c) a plurality of downstream compressors or compression turbo-machines disposed in a series arrangement with the at least one initial compression stage.
  • the speed of the variable speed motor is adjusted to increase or decrease the flow rate of the ambient pressure air to the at least one air compressor and the flow rates of the compressed air to the plurality of downstream compressors or compression turbo-machines toward a desired flow rate.
  • the speed of the variable speed motor remains situated above or remains situated below a restricted speed zone.
  • the present invention may also be characterized as a method for compressing air, comprising the steps of: (i) receiving a flow of ambient pressure air to at least one air compressor having at least one initial compression stage; (ii) driving the at least one air compressor having at least one initial compression stage with a variable speed motor having at least one shaft; (iii) compressing the flow of ambient pressure air in the at least one air compressor thereby producing a flow of compressed air exiting the at least one air compressor at a first pressure; (iv) further compressing the flow of compressed air at the first pressure to a higher pressure in a plurality of downstream compressors or compression turbo-machines disposed in a series arrangement with the at least one initial compression stage; and (v) adjusting the speed of the variable speed motor to increase or decrease the flow rate of the ambient pressure air to the at least one air compressor and the flow rates of the compressed air to the plurality of downstream compressors or compression turbo-machines toward a desired flow rate.
  • the compression train system and method may include a first centrifugal compressor is mounted on one end of the shaft of the variable speed motor to form a first of the two stages of compression configured to compress the ambient pressure air to a first pressure; and a second centrifugal compressor is mounted on the other end of the shaft and in flow communication with the first centrifugal compressor to form a second of the two stages of compression to further compress the air to a second pressure, higher than the first pressure.
  • the compression train system and method may include a first centrifugal compressor is mounted on one end of the shaft of the variable speed motor to form a first of the two stages of compression and configured to compress a first portion of the ambient pressure air to a first pressure; and a second centrifugal compressor is mounted on the other end of the shaft to form a second of the two stages of compression and configured to compress to also compress a second portion of the ambient pressure air to the first pressure.
  • the present invention provides a method of producing a compressed gas and controlling flow rate of the compressed gas in which the gas is compressed within a compression system having at least one stage of compression to compress a gas and thereby to produce the compressed gas and an electric motor directly coupled to the at least one stage of compression.
  • the motor has a restricted speed zone within which vibrational modes can damage the compression system. More specifically, the damage to the compression system can be damage to the motor and/or the compressor coupled to the motor.
  • the at least one stage of compression can comprise a centrifugal compressor having inlet guide vanes to control the flow rate of the compressed gas to a desired flow rate and the electric motor can have a speed controller to control the speed of the motor and therefore, an impeller of the centrifugal compressor to also control the flow rate of the compressed gas to the desired flow rate.
  • the desired flow rate is able to be obtained with the speed of the electric motor situated above or below the restricted speed zone, the flow rate is controlled to achieve the desired flow rate by controlling the speed of the electric motor with the speed controller and with the inlet guide vanes set at a 0° swirl angle.
  • the term “0° swirl angle” when used in connection with the position of the inlet guide vanes means that the vanes are set a wide open position such that the flow out of the inlet guide vanes is parallel to a centerline of the flow which commonly would be the centerline of a pipe feeding the gas to the inlet of the compressor.
  • the speed of the electric motor is controlled with the speed controller such that the speed is set at an upper speed, above the restricted speed zone and the inlet guide vanes are set to obtain the desired flow rate.
  • the flow rate of the compressed gas can be measured downstream of the compression system to obtain a measured flow rate.
  • the measured flow rate can be compared with the desired flow rate to obtain an error in the desired flow rate if a difference between the measure flow rate and the desired flow rate exists.
  • the error in the desired flow rate is minimized by adjusting the speed of the electric motor with the speed controller.
  • the error in the desired flow rate is minimized by adjusting the inlet guide vanes.
  • the speed of the electric motor is decreased in decreasing speed steps.
  • the inlet guide vanes are successively opened during each of the decreasing speed steps such that the inlet guide vanes are set at the 0° swirl angle at a lower speed, below the restricted speed zone. The speed is thereafter, decreased until the new speed is obtained.
  • the position of the inlet guide vanes required to obtain the desired flow rate at the upper speed, above the restricted speed zone is calculated.
  • the speed of the electric motor, with the inlet guide vanes set at the 0° swirl angle is set at the lower speed, below the restricted speed zone.
  • the speed of the electric motor is increased in increasing speed steps until the upper speed, above the restricted speed zone is obtained.
  • the inlet guide vanes are successively closed during each of the increasing speed steps such that the position of the inlet guide vanes required to obtain the desired flow rate will be reached when the upper speed, above the restricted speed zone, is reached.
  • the successive closing of the inlet guide vanes would impart more swirl to the flow entering the compressor and therefore, decrease the flow rate to the desired flow rate.
  • the electric motor can be a high speed permanent magnet motor and the speed controller can be a variable frequency drive.
  • the compression system can have two stages of compression to compress the gas.
  • the centrifugal compressor is a first centrifugal compressor mounted on one end of a motor shaft of the high speed permanent magnet motor to form a first of the two stages of compression and to compress the gas to a first pressure.
  • a second centrifugal compressor, in flow communication with the first centrifugal compressor, is mounted on the other end of the motor shaft to form a second of the two stages of compression to further compress the gas to a second pressure, higher than the first pressure.
  • the compression system can have two centrifugal compressors having a common feed through which the two centrifugal compressors are fed with the gas and a common outlet from which the compressed gas is discharged.
  • the centrifugal compressor is a first of the two centrifugal compressors mounted on one end of a motor shaft of the high speed permanent magnet motor and a second of the two centrifugal compressors is mounted on the other end of the motor shaft.
  • Each of the first and the second of the two centrifugal compressors have the inlet guide vanes.
  • the present invention also provides an apparatus for producing a compressed gas and controlling flow rate of the compressed gas.
  • the apparatus comprises a compression system having at least one stage of compression to compress a gas and thereby to produce the compressed gas.
  • An electric motor directly coupled to the at least one stage of compression, has a restricted speed zone within which vibrational modes can damage the compression system.
  • the at least one stage of compression can comprise a centrifugal compressor having inlet guide vanes responsive to an inlet guide vane positioning signal to control the flow rate of the compressed gas to a desired flow rate and the electric motor has a speed controller responsive to a speed control signal to control the speed of the motor and therefore, an impeller of the centrifugal compressor to also control the flow rate of the compressed gas to the desired flow rate.
  • a master controller generates the inlet guide vane signal and the speed control signal.
  • the master controller is programmed to calculate a calculated speed of the electric motor to obtain the desired flow rate and an inlet guide vane position at a speed level at an upper speed, above the restricted speed zone that will obtain the desired flow rate. Additionally, the master controller is also programmed to generate the speed control signal such that the speed control signal is referable to the calculated speed when the calculated speed is situated above or below the restricted speed zone and generate the inlet guide vane positioning signal such that the inlet guide vanes will be set at the 0° swirl angle.
  • the master controller is also programmed to generate the speed control signal such that the speed control signal will be referable to the speed level at an upper speed, above the restricted speed zone and the inlet guide vane positioning signal will be referable to the inlet guide vane position that will obtain the desired flow rate.
  • a flow transducer is situated downstream of the compression system and is configured to generate a flow signal referable to the actual flow rate of the compressed gas.
  • the master controller is responsive to the flow signal and is also programmed to compare the actual flow rate with the desired flow rate and generate an error in the desired flow rate if a difference between the actual flow rate and the desired flow rate exists.
  • the speed signal is generated to minimize the error in the desired flow rate and when the desired flow rate is not able to be obtained without the calculated speed being situated within the restricted speed zone, the inlet guide vane positioning signal is generated to minimize the error in the desired flow rate.
  • the master controller is programmed such that when a current speed of the electric motor is situated at the upper speed, above the restricted speed zone and the desired flow rate is currently obtained by adjusting the inlet guide vanes to a current position of the inlet guide vanes and the calculated speed of the electric motor required to obtain a new desired flow rate is below the restricted speed zone, the speed control signal is successively generated to be referable to successively decreasing speeds of the electric motor in decreasing speed steps until a lower speed, below the restricted speed zone, is obtained.
  • the inlet guide vane positioning signal is successively generated during each successive generation of the speed control signal to be referable to successively greater openings of the inlet guide vanes such that the inlet guide vanes are set at the 0 ° swirl angle at a lower speed, below the restricted speed zone.
  • the speed control signal is generated such that the calculated speed is obtained.
  • the position of the inlet guide vanes required to obtain the desired flow rate at the upper speed, above the restricted speed zone is calculated, the speed control signal is generated to be referable to the lower speed, below the restricted speed zone, the speed control signal is successively generated to be referable to successively increasing speeds of the electric motor in increasing speed steps until the upper speed, above the restricted speed zone is obtained.
  • the inlet guide vane positioning signal is generated during each of the increasing speed steps to be referable to successively closed positions of the inlet guide vanes such that the position of the inlet guide vanes required to obtain the desired flow rate will be reached when the upper speed, above the restricted speed zone, is reached.
  • the electric motor can be a high speed permanent magnet motor and the speed controller can be a variable frequency drive.
  • the compression system can have two stages of compression and the centrifugal compressor is a first centrifugal compressor mounted on one end of a motor shaft of the high speed permanent magnet motor to form a first of the two stages of compression.
  • a second centrifugal compressor, in flow communication with the first centrifugal compressor, is mounted on the other end of the motor shaft to form a second of the two stages of compression.
  • the compression system can have two centrifugal compressors having a common feed through which the two centrifugal compressors are fed with the gas and a common outlet from which the compressed gas is discharged.
  • the centrifugal compressor is a first of the two centrifugal compressors mounted on one end of a motor shaft of the high speed permanent magnet motor and a second of the two centrifugal compressors is mounted on the other end of the motor shaft.
  • Each of the first and the second of the two centrifugal compressors have the inlet guide vanes and each are responsive to the inlet guide vane positioning signal.
  • FIG. 1 is a schematic diagram of a compression system for carrying out a method in accordance with the present invention
  • FIG. 2 is a graphical representation of speed dependent natural rotor frequencies at first and second bending modes for an electric motor utilized in the compression system of FIG. 1 .
  • FIG. 3 is the graphical representation of speed dependent natural rotor frequencies of FIG. 2 with restricted speed zones indicated by shaded areas;
  • FIG. 4 is a compressor map of the compressor used in the first stage of compression of the compression system shown in FIG. 1 ;
  • FIGS. 5A and 5B are a logic flow diagram of the programming utilized in the master controller of the compression system of FIG. 1 ;
  • FIG. 6 is a logic flow diagram of the programming utilized in an IGV Positioning Subroutine For Speeds Below The Restricted Speed Zone shown in FIG. 5 ;
  • FIG. 7 is a logic flow diagram of the programming utilized in a Restricted Speed Zone IGV Positioning Subroutine I shown in FIG. 5 ;
  • FIG. 8 is a logic flow diagram of the programming utilized in a Restricted Speed Zone IGV Position Subroutine II shown in FIG. 5 ;
  • FIG. 9 is a logic flow diagram of the programming utilized in a Feedback Subroutine shown in FIGS. 5 ;
  • FIG. 10 is an alternative embodiment of a compression system for carrying out a method in accordance with the present invention.
  • a compression system 1 in accordance with the present invention is illustrated.
  • a gas by way of a gaseous feed stream 10 is compressed in a first compressor 12 having inlet guide vanes 14 to adjust the flow rate of the gas to be compressed.
  • First compressor 12 constitutes a first stage of compression.
  • the gas is further compressed in a second compressor 18 to a higher pressure to produce a compressed gas stream 20 .
  • First and second compressors 12 and 18 are centrifugal compressors of known design having an inlet, an impeller, a diffuser and a scroll-like volute to discharge the gas after having been compressed.
  • the first and second compressors 12 and 18 are connected to oppose ends of a motor shaft 22 of a motor 24 that drives the impellers of such compressors.
  • Motor 24 can be a high speed permanent magnet motor.
  • the speed of permanent magnet motor 24 is controlled by a variable frequency drive 26 that can adjust the speed of the motor 24 and therefore, also the flow rate of the compressed gas stream 20 .
  • Variable frequency drive 26 is linked to the motor 24 by an electrical connection 28 .
  • the variable frequency drive 26 is responsive to a speed control signal referable to a motor speed that is generated in a master controller 30 and transmitted to the variable frequency drive by an electrical connection 32 .
  • electrical connections 28 and 32 are provided between the motor 24 , the variable frequency drive 28 , and the master controller 30 to transmit a signal referable to the speed of the motor 24 to in effect allow the programming employed in master controller 30 to measure the actual speed of the motor 24 .
  • sensors related to such bearings would be capable of sending such a signal and is conventional.
  • the master controller 30 also generates an inlet guide vane position signal that is transmitted to a positioner incorporated into the inlet guide vanes 14 by means of an electrical connection 34 .
  • the positioner also generates a signal proportional to the position of the inlet guide vanes that is fed back to the master controller 30 to enable the programming logic employed in the master controller 30 to in effect measure the position of the inlet guide vanes 14 .
  • the positioner and the inlet guide vanes 14 and its features discussed above are conventional and well known in the art.
  • the master controller 30 is responsive to a flow request 36 for the compressed gas stream 20 that serves as an input 38 to the master controller 30 .
  • motor 24 has a restricted speed zone in which operation can only be conducted for a brief period of time without vibrational modes occurring that can damage the motor and/or the first and second compressors 12 and 18 .
  • master controller 30 When a desired flow rate is able to be obtained by speed control without the speed of motor 24 residing within the restricted speed zone, master controller 30 generates a speed control signal in response to the flow request 36 that will produce a speed within the motor 24 that will in turn produce the desired flow rate of the compressed gas stream 20 .
  • the inlet guide vane signal is generated by the master controller 30 to fully open the inlet guide vanes 14 or in other words, set the inlet guide vanes 14 to the 0° swirl position.
  • the speed signal is generated by the master controller 30 to set the speed of the motor 24 to the upper speed, above the restricted speed zone and the inlet guide vane signal is generated to close the inlet guide vanes to produce the desired flow rate or in other words, impart more swirl to the incoming flow to the first compressor 12 and thereby decrease the flow rate to the desired flow rate.
  • feedback can be provided by a flow transducer 40 that generates a flow signal, referable to the flow of the compressed gas stream 20 , that is inputted into the master controller 30 by an electrical connection 42 should there be a difference between the measured flow rate and the flow request 36 .
  • the master controller 30 either further adjusts the speed of the permanent magnet motor 24 or the inlet guide vanes 14 or both to minimize the error.
  • the present invention is described with reference to a high speed permanent magnet motor, it would have equal applicability to other high speed motors controlled by a variable frequency drive such as an induction motor and a switched reluctance motor. Further, although two compression stages are illustrated in FIG. 1 , the present invention would have equal applicability to a single compression stage provided by a compressor connected to the shaft of an electric motor.
  • first and second bending motor shaft modes In an electric motor that is directly coupled to a centrifugal compressor either at one end of a motor shaft or where two centrifugal compressors are directly coupled to opposite ends of the rotor shaft, there are speed dependent natural frequencies for first and second bending motor shaft modes in which extended operation at such speed can damage the electric motor.
  • the bending modes have both forward and backward precession modes “F” and “B”.
  • the first bending mode has two nodes (shown by the triangles) that are typically located near the journal bearings supporting the motor shaft 22 for rotation.
  • the second bending mode has three nodes, with the outer two nodes being typically located near such journal bearings and a central node located between the two outer nodes and between the two bearings.
  • Excitation of the forward modes is most commonly created by rotor unbalance and non linear stiffness effects in the bearings, also known as cross coupling.
  • Excitation of the backward modes is most commonly created by the motor shaft rubbing stationary parts such as shaft seals. Due to the ever presence of unbalance and cavity cross coupling of the forward mode, as compared with a typically brief rub event of the backward mode, greater concern is typically given to the forward processing modes while the backward modes are, in many situations ignored or discounted. Therefore, excitation amplitudes for forward modes are more prone to grow to unacceptable levels when compared to the brief rubs exciting the backward modes and can present more of an operational concern.
  • journal bearings that can be magnetic type bearings and which are provided within a motor casing.
  • hydrodynamic and airfoil type bearings are also possible.
  • a thrust bearing that can also can be a magnetic or also, possibly a hydrodynamic or airfoil type of bearing, is provided to absorb axial loadings.
  • the first and second compressors 12 and 18 are connected to the motor housing of the permanent magnet motor 24 and, as indicated above, the motor shaft 22 drives two impellers located in the first and second compressors 12 and 18 situated at opposite ends of the motor shaft 22 . This collection of rotating parts is referred to as the rotor.
  • the rotor In a forward bending mode, as the shaft starts to vibrate and precess in the direction of rotation, the rotor can contact the internal stationary parts within the motor casing resulting in potential damage or destruction of the motor.
  • separation margins are placed on the rotor natural frequencies shown in FIG. 1 .
  • representative, yet arbitrary values of separation margin for each mode are listed in FIG. 3 next to the abbreviation SM.
  • the actual separation margins used are typically a function of the amount of damping present as well as experience or industrial guidelines. For instance, the American Petroleum Institute provides such guidelines in its publication API 684 . It is to be noted that the rotor natural frequencies shown in this illustration are a product of analytical calculations made during the design phase of the motor. Consequently, these are predicted dynamic responses that have a degree of uncertainty.
  • the diagonal line is referred to as an operating line that has a slope of 1 to conveniently ascertain the bounds of such restricted speed zones.
  • the rotor natural frequency plots in FIGS. 1 and 2 are exemplary only and such plots will vary in different motors.
  • the backward precession mode in the second bending mode is to be avoided.
  • this is of less concern and therefore, the safety margin is often selected to be less than the forward precession mode of the first bending mode.
  • the motor need only operate at 9000 rpms.
  • this motor speed will represent an upper limit of operation.
  • there could be three restricted speed zones namely both the forward precession mode of the first bending mode, the backward precession mode of the second bending mode and the forward precession mode of the second bending mode.
  • there is one restricted speed zone and the same would lie between, but would not include, 6300 and 6800 rpms.
  • this restricted speed zone represents 12.5 percent of the operational speed range of the motor that would be unavailable for regulating the flow rate of one or more compressors connected to the motor.
  • a compressor map is shown for the compressor 12 .
  • the compressor is capable of delivering a flow rate from between 12 and 30 LBM/Sec (pound mass per second) of flow over the operating speed range.
  • LBM/Sec compound mass per second
  • the restricted speed zone prevents delivery of mass flows from 19 LBM/Sec to 21 LBM/Sec or in other words about 17 percent of the range of flow rates to be delivered by manipulation of speed alone.
  • the master controller 30 is programmed with a control program, with specific reference to FIG. 5A , the control program begins execution at the execution stage 50 “Begin” with the input a new flow rate “Q S ” specified in execution stage 52 through input of a flow request 36 as illustrated in FIG. 1 .
  • the current flow rate “Q R ” is measured by flow transducer 40 and is input into execution stage 54 along with the current speed of the N R that is preferably stored as data within the controller 30 .
  • a flag, “Feedback” is set to “off” in stage 55 and the program then proceeds to execution stage 56 in which data contained in a compressor map of the type illustrated in FIG. 4 is obtained to determine the speed of the compressor with the inlet guide vanes 14 set at 0°. This speed is referred to by the variable N S .
  • the program then proceeds to execution stage 58 to perform a test to determine whether the new speed, “N S ” is outside the minimum or maximum speed of the first compressor 12 .
  • the minimum and maximum speed of the compressor would be in a range from 5000 and 9000 rpms. If the answer to the test is yes, then execution stage 60 executes and a message is sent to the operator that the requested flow rate is out of range.
  • execution stage 62 executes in which a test is performed to determine whether the new speed is in the restricted speed zone which in the example given above would be between 6300 and 6800 rpms. If the answer to the test is no, then execution stage 64 executes in which a further test is performed to determine whether the current speed N R is at an upper speed, above the restricted speed zone. In the example, the upper speed would be 6800 rpms since the restricted speed zone lies below this speed. It is to be noted, that such upper speed could be set higher than 6800 rpms, for instance 7000 rpms to provide even a greater margin than that calculated for the specific motor.
  • a speed signal is generated by the master controller 30 which, as indicated in execution stage 66 is sent via electrical connection 32 to the variable frequency drive 26 to in turn set the motor 24 to the speed referable to the speed signal.
  • the program then proceeds to a “Feedback Subroutine” 68 and then to the end of program execution as designated by reference number 70 .
  • two variables “IGV” and “IGV S ” are both set to 0 as shown at 67 and 71 , respectively.
  • the setting of the current position of the inlet guide vanes 14 “IGV” and the specified position thereof “IGV S ” at 0 is necessary to allow the Feedback Subroutine 68 to properly execute and define a new reference inlet guide vane position “IGV R ” to be equal to 0.
  • the Feedback Subroutine 68 allows the speed of the motor 24 or the position of inlet guide vanes 14 to be adjusted as required to obtain the new flow rate Q S should the measured flow rate that is obtained not be equal to Q S .
  • Feedback Subroutine 68 is optional.
  • test in execution stage 64 is yes, then another test is performed in execution stage 72 . If as indicated in execution stage 72 , the test produces a negative answer, then only the speed of the motor 24 need be adjusted with a 0° swirl angle of the inlet guide vanes 14 , in other words, fully open, to obtain the desired flow rate of the compressed gas stream 20 . Reviewing the logic, as indicated in execution stage 62 , the new speed is not in the restricted speed zone, the current speed is in a restricted speed zone as tested in execution stage 64 and since the new speed as tested in the execution stage 72 is not below the restricted speed zone, the new speed must be above the restricted speed zone.
  • an inlet guide vane positioning signal is generated to reposition the inlet guide vanes 14 to the 0° swirl angle so that no swirl is generated and a speed control signal is generated that is referable to the desired speed that will obtain the desired flow rate.
  • These signals are transmitted to the variable frequency drive 26 and to the inlet guide vanes 14 by electrical conductors 32 and 34 , respectively. Since the positioning of the inlet guide vanes 14 is not instantaneous, a loop is performed in which a signal referable to the inlet guide vane position is transmitted from inlet guide vanes 14 back to the master controller through electrical connection 34 to measure the current position of the inlet guide vanes 14 as indicated in execution stage 76 .
  • execution stage 78 a test is performed as shown in execution stage 78 in which the measured inlet guide vanes position is tested against the 0° desired position. If the answer to the test is no, the execution of the control program loops back to execution stage 76 until the desire position IGV M of 0° is reached or in other words, until the test performed in execution stage 78 can be answered in the affirmative. Thereafter, the program executes a loop in which the speed “N” of the motor 24 is measured at 79 and the speed is then tested in stage 80 to determine whether the measured speed has reached N S , the specified speed. If the motor 24 has not reached the specified speed, the program loops back to 79 until the measured speed has in fact reached the specified speed.
  • variable “IGV S ” is set to 0 and the programming proceeds to the Feedback Subroutine 68 and then the program end 70 .
  • the setting of the variable “IGV S ” to 0 supplies a necessary variable to the Feedback Subroutine 68 to allow it to properly execute.
  • an IGV Positioning Subroutine for Speed Below the Restricted Speed Zone 82 executes.
  • both the speed of the motor 24 is incrementally decreased while within the restricted speed zone and the inlet guide vanes 14 are incrementally opened to the 0° swirl angle.
  • the speed of the motor is also adjusted to obtain the desired flow rate Q S .
  • the subroutine generally shown at 82 initiates with a lookup of the upper Speed N U , above the restricted speed zone and then a look up of the lower speed N L , below the restricted speed zone as indicated at 83 and 84 , respectively.
  • This “lookup” can be performed by simply reading data referable to these values, namely, 6300 and 6800 rpms. The user is able to select the number of steps that the speed will be dropped or these may be pre-programmed. In any case, assuming a user selected speed step, the same will be an input into the control program of the master controller 30 and will have a value of “K”.
  • the program then performs a calculation to determine the incremental speed drop for the motor 24 by subtracting the lower speed, below the restricted speed zone “N L ” from the upper speed, above the restricted speed zone “N U ” and dividing the difference by the number of steps “K” that the user has selected. Thus, assuming 10 steps were selected by a user, then the speed will be adjusted in decreasing steps of 50 rpms.
  • the position of the vanes “IGV C ” of the inlet guide vanes 14 is then measured by transmitting the value from the inlet guide vanes 14 to the master controller 30 as shown at 88 .
  • an incremented speed N i is sent to the motor 24 by means of a speed signal referable thereto generated by the programming in the master controller 30 and sent to the variable frequency drive 26 as indicated in execution stage 90 .
  • the first increment N i is set equal to 6750 rpms.
  • the required position of the inlet guide vanes is calculated at execution stage 92 . This is simply a ratio of the difference between the current incremental speed value N i and N L to the speed range of the restricted speed zone, namely N u -N L .
  • the speed of the motor 24 is measured at 98 . Further, since the positioning of the inlet guide vanes is also not instantaneous, the program loops between a step in the programming 100 in which the position of the vanes in the inlet guide vanes 14 is measured by transmittal to the master controller 30 and then a test is performed at 102 to determine whether the inlet guide vanes 14 are at the position calculated at execution stage 92 of the programming. If the result of the test of 102 is negative, then execution stage 100 is re-executed until the test is positive.
  • a further test is performed in execution stage 104 to determine whether the speed of the motor 24 , that is obtained in execution stage 98 , has reached the incremented speed N i . If the answer is in the negative, the programming loops back to execution stage 98 . If the test of 104 is positive, or the measured speed has reached the incremented speed, then as set forth in execution stage 106 , the speed is tested to determine whether the speed measured in stage 98 has reached the lower speed, below the restricted speed zone N L . If the answer to such test is no, then the speed is incremented to a new value of N i as indicated in execution stage 108 .
  • the next increment in a user specified 10 step routine would be 6700 rpms, assuming a 50 rpm increment.
  • the program would then loop back to execution stage 90 to set the new increment in the speed to the motor 24 . If, however, the answer to the test of execution stage 106 is in the affirmative, the inlet guide vanes 14 are set in the fully open position and at the 0° swirl angle.
  • a speed signal is generated that will send the required speed to produce the desired flow, as determined in execution stage 56 , to the variable frequency drive 26 to set the motor 24 at such speed.
  • the programming will then proceed to a loop in which the speed is measured in stage 110 and then tested in 111 to determined whether the measured speed has reached the specified speed N S .
  • the variable IGV S is set equal to IGV as indicated in step 112 and the programming proceeds to the Feedback Subroutine 68 and program end 70 .
  • the setting of “IGV S ” to be equal to “IGV” allows the Feedback Subroutine 68 to properly execute.
  • execution stage 113 is next executed as shown in FIG. 5B .
  • Execution stage 113 tests whether the current speed is at the upper speed N U , above the restricted speed zone. Assuming it is not and therefore, the answer to the test is no, then the current speed can either be above or below the restricted speed zone. This is determined in execution stage 114 and assuming that the answer to the test is no, then, the Restricted Speed Zone IGV Positioning Subroutine I is executed as set forth at 115 . In this subroutine, the speed of motor 24 will be set at the upper speed above the restricted speed zone and the desired flow rate will be obtained with the inlet guide vanes 14 to impart the requisite swirl to the flow.
  • the logic employed in the programming of the subroutine of 115 begins at execution stage 116 with a lookup of the upper speed “N U ”, above the restricted speed zone which in the example is 6800 rpms. Again, for purposes that will be discussed, the specified speed variable N S is set to N U at 117 . A speed signal is then generated by the master controller 30 which is transmitted to the variable speed drive 26 and the motor 24 is set to operate at such speed as set forth in execution stage 118 . Since the speed was above the upper speed, above the restricted speed zone, the motor 24 must decelerate.
  • a loop is executed in which the speed of the motor 24 is measured at 120 and then a test is performed in execution stage 122 to determine whether the motor 24 has reached the upper speed above the restricted speed zone.
  • the programming proceeds to 124 where a lookup is performed in a lookup table to determined the position of vanes in inlet guide vanes 14 to obtain the new flow rate that has been requested as set forth at reference number 36 in FIG. 1 and in particular, the execution stage 52 of the programming.
  • the dashed lines represent possible swirl angle positions of the inlet guide vanes 14 to obtain the desired flow rates at a speed set at the upper limit of the restricted speed zone.
  • the position selected would be at the intersection of the dashed lines with the system resistance line at which pressure ratios and mass flow are obtained at specific compressor speeds.
  • compressor vane positions of between 0° and 20° would be available to obtain the desired flow rates within the restricted speed zone.
  • Data concerning the vane positions and mass flow would be stored in the look up table and points between actual stored data could be interpolated.
  • an inlet guide vane positioning signal is computed for the inlet guide vanes 14 at 126 and the signal is then sent to the inlet guide vanes 14 at 128 from the master controller 30 . Since the positioning of the inlet guide vanes 14 is not instantaneous, a loop is performed in which the position of the vanes within the inlet guide vanes 14 is measured at 130 and a test is performed at 132 to determine whether the inlet guide vanes 14 are at the position to obtain the desired flow rate. When the answer to the test is yes, then the programming proceeds to the feed back subroutine 68 and then to end 70 .
  • the programming contained in the Restricted Speed Zone IGV Positioning Subroutine II 134 is executed.
  • the speed of the motor is increased to the lower speed below the restricted speed zone and then the speed is incrementally increased until the upper speed above the restricted speed zone is reached.
  • the inlet guide vanes 114 are incrementally closed until a position is reached at which the desired flow rate will be obtained with the speed of the motor 24 at the upper speed, above the restricted speed zone.
  • the subroutine 134 is programmed so that first the lower speed, below the restricted speed zone “N L ” is determined in execution stage 136 .
  • a speed signal referable to the lower speed “N L ” is then generated by the master controller 30 and transmitted to the variable frequency drive 26 to adjust the speed of the motor 24 to such speed as indicated in execution stage 138 . Since the acceleration of the motor 24 is not instantaneous, a loop is then performed in which the speed of the motor 24 is measured at 142 and then tested in execution stage 143 to determine whether the motor speed has reached the lower speed, below the restricted speed zone.
  • a lookup in a lookup table is performed in execution stage 144 to determine the positioning of the inlet guide vanes 14 to obtained the desired flow rate of the compressed gas stream 20 at the upper speed, above the restricted speed zone by means of the use of data of the type mentioned above with respect to FIG. 4 .
  • the variable “N S ” is set to the upper speed variable “N U ” at 145 .
  • the user as in input to the master controller 30 can specify a number of steps “K” to increment the speed to raise the speed of the motor 24 from the lower speed, below the restricted speed zone to the upper speed, above the restricted speed zone.
  • This speed increment is given by the difference between the uppermost and lower speeds divided by the increment. For instance, in the example above, if ten increments were desired, then the speed increment would be 50 rpms. For example, assuming that the speed is at the lower level of 6300 rpm and ten fifty rpm steps have been selected, first speed increment “N I ” is set equal to 6350 rpm.
  • a speed signal is generated referable to the incremented speed, “N i ” that is generated by the master controller 30 and transmitted to the variable frequency drive 26 to set the motor to the incremented speed.
  • the position of the inlet guide vanes 14 is also incremented by a ratio multiplied by the required inlet guide vane position “IGV S ” of the inlet guide vanes 14 in execution stage 150 . This ratio is between a difference between the current value of N i and the lower speed level of the restricted speed zone (N i— N L ) divided by the difference between the uppermost and lower speeds of the restricted speed zone (N U -N L ).
  • the ratio will be equal to 1 and the inlet guide vane position will be equal to IGV S .
  • the incremental value of the inlet guide vane position IGV i determined at 150 is then used to lookup or compute an inlet guide vane positioning signal in execution stage 152 that will be generated by master controller 30 . This signal is sent to inlet guide vanes 14 in execution stage 154 to incrementally close the inlet guide vanes 14 .
  • the programming then executes a loop in which the speed of the motor 24 and position of the inlet guide vanes 14 are measured in 156 and 158 , respectively. Then a test is performed in execution stage 160 to determine whether the measured position of the inlet guide vanes 14 has reached the value calculated in execution stage 150 . When the answer to this test is yes, then the measured speed N is compared to the incremented speed N i at 162 . If the answer to the test is in the negative, the programming loops back to 156 . If the answer to the test of 160 is in the affirmative, then a test is performed at 164 to determine whether the measured speed has reached the upper speed above the restricted speed zone “N U ”.
  • a lookup is performed at 170 to determine “N U ”, the upper speed, above the restricted speed zone.
  • the variable N S is set equal to N U at 172 and the flag “Feedback” is tested at 174 as to whether it is set “Off”. If the answer to this question is yes, as would be the case if the feed back subroutine were not reached directly before the time of such test, a lookup is performed at 176 in a lookup table to determine the required position of the inlet guide vanes 14 in a manner discussed above with respect to the type of data shown in FIG. 4 .
  • the required inlet guide vane positioning signal is either determined from a lookup table or computed.
  • the inlet guide vane positioning signal is then generated by master controller 30 and sent to inlet guide vanes 14 in execution stage 180 .
  • a loop is then executed wherein the position of the inlet guide vanes 14 is measured at 182 and a test is performed to determine whether the measured value has reached the required position of the inlet guide vanes at 184 .
  • the programming proceeds to the feed back subroutine 68 and then the program end 70 .
  • the inlet guide vanes 14 are being opened in a ratio related to the current incremented speed. It is possible, however, that such incremental opening could be by a fixed percentage and the speed could be incremented by a fixed percentage. However, as can be appreciated, if this were done, then either required speed would be reached before the required inlet guide vane opening or vice-versa. In such case programming would also have to be provided to obtain the required speed or inlet guide vane opening in a percentage that completed the speed or required opening. Such final percentage would differ from the fixed percentage. At the other extreme it is also possible to simply open the inlet guide vanes to the 0° position while sending a speed command to the motor 24 at which the motor will runs at the speed N s that will produce the desired flow rate.
  • feed back control may be executed by the Feedback Subroutine 68 to make certain that the measured flow rate “Q” has in fact reached the specified flow rate “Q S ”. It is to be noted that an embodiment of the present invention is possible that does not use such feed back control and would depend on calculated values for control of flow rate. However, assuming such feed back control is employed, as indicated, the flow rate is measured at 186 by such means as the flow transducer illustrated in FIG. 1 and a test is performed at 188 to determine whether the “Q” is equal to “Q S ”. If this has in fact occurred, then the programming proceeds to end 70 and no feed back control is required.
  • N S the specified speed of the motor 24
  • Q S -Q the specified speed of the motor 24
  • Q-Q R the reference flow rate
  • IGV NS is the current specified value of the inlet guide vanes 14 , or IGV S either increased or decreased by the same ratio of flow rates used in the calculation of the new specified speed multiplied by a difference between IGV S and IGV R .
  • the new specified position of the inlet guide vanes 14 is then redefined in execution stage 202 . It is to be noted that if the programming has proceeded from execution stages 67 and 71 or from execution stage 81 or from subroutine 82 , then IGV NS will remain at 0 or in other words, the 0° swirl angle. If the programming has proceeded from subroutines 115 and 134 or execution stage 184 , the value of IGV S will be that value defined in such subroutines or execution stage 184 .
  • a new reference speed, reference flow rate and reference IGV position are defined by the current measured speed of the motor 24 , the current measured flow rate and the current measured position of the inlet guide vanes 14 .
  • the programming than loops back to execution stage 58 .
  • the speed of the motor 24 will be adjusted in execution stage 66 , subsequent to the feed back subroutine 68 by either increasing or decreasing the speed of the motor until Q is equal to Q S .
  • the speed in such case is adjusted to minimize the error in the flow.
  • N S will be in the restricted speed zone and the current speed of the motor will be at the upper speed level N U , above the restricted speed zone.
  • the answer to the test of execution stage 113 would be “yes”.
  • the flag “feedback” would be set to “on”.
  • execution stage 176 would be by-passed as the answer to the test of execution stage 142 would be yes, and the value of IGV S to be sent to the inlet guide vanes 14 would be IGV NS developed in execution stage 200 of the feed back subroutine 68 .
  • the flow rate error would be minimized by adjusting the inlet guide vanes 14 .
  • the present invention has applicability to a compression system 1 ′ in which the compressed air stream 10 is introduced into two compressors 12 a and 12 b from dual feeds 206 to produce a compressed gas stream 20 ′ from dual outlets 208 .
  • the compressors 12 a and 12 b are mounted on the ends of the motor shaft 22 of the motor 24 and are provided with inlet guide vanes 14 a and 14 b that are controlled through electrical connections 34 a and 34 b that transmit inlet guide vane positioning signals thereto from the master controller 30 .
  • Electrical connections 34 a and 34 b also transmit signals from the inlet guide vanes 14 a and 14 b back to the master controller 30 to indicate the position of vanes within the inlet guide vanes 14 a and 14 b.
  • the programming to control the speed of motor 24 and the position of vanes within inlet guide vanes 14 a and 14 b could be the same as outlined above with respect to the compression system 1 discussed above with identical inlet guide vane positioning signals sent to inlet guide vanes 14 a and 14 b and with the programming reacting to the position of the vanes of one of the inlet guide vanes 14 a and 14 b since the same would be identical units.
  • the speed signal would be generated in an identical manner to control the speed of motor 24 to that outlined above with such speed set at the uppermost limit of the restricted speed zone where a flow request were generated that would otherwise require a motor speed within the restricted speed zone and with the flow rate adjusted by the inlet guide vanes 14 a and 14 b.

Abstract

A compression train system and method for compressing air for an air separation unit is provided. The system includes at least one initial air compressor configured to receive and compress a flow of ambient pressure air and driven by a variable speed motor. The system further includes a plurality of downstream compressors or compression turbo-machines disposed in a series arrangement with the at least one initial compression stage. The desired flow rates to the compression system is controlled by adjusting the speed of the variable speed motor and the position of inlet guide vanes to increase or decrease the flow rate of the ambient pressure air and keep the speed of the variable speed motor above or below a restricted speed zone.

Description

    CROSS REFERENCE TO RELATED APPLICATIONS
  • The present application is a continuation application and claims the benefit of and priority to U.S. patent application Ser. No. 13/644,066 filed on Oct. 3, 2012, the disclosure of which is incorporated by reference herein.
  • FIELD OF THE INVENTION
  • The present invention relates to a method and apparatus for producing a compressed gas and for controlling the flow rate of the compressed gas in which a compressor is directly coupled to an electric motor and a restricted speed zone exists where vibrational modes can damage the electric motor and/or the compressor. More particularly, the present invention relates to such a method and apparatus in which a desired flow rate is obtained by controlling the speed of the electric motor when such flow rate can be obtained by a speed that is not within the restricted speed zone and through inlet guide vane manipulation when such flow rate would otherwise be obtained by a speed within the restricted speed zone.
  • BACKGROUND OF THE INVENTION
  • Gases are typically compressed in compressors that are driven by electric motors. The compressors can be connected so that the gas is compressed in stages from ambient to a high delivery pressure. Interstage cooling is employed to remove the heat of compressor between stages. A common compressor design that is utilized is a centrifugal compressor. In a centrifugal compressor, the gas to be compressed enters an inlet and is compressed by action of an impeller that is rotated by the electric motor. The gas then passes through a diffuser and is discharged from a volute of spiral-like configuration.
  • In many industrial processes employing compressors, it is necessary to reduce or increase the flow rate of the gas to be compressed from a design level of flow rate. For instance, in cryogenic air separation, air is compressed in a series of compression stages, cooled to a temperature suitable for the rectification of the air and then introduced into a distillation column system to separate the air into its component parts, for instance, oxygen, nitrogen and argon. In order to optimize the margin in the sale of separated products, it is important that electrical energy costs be minimized. Since, the cost of electrical power will vary with the time of day, it is most cost efficient to conduct the air separation at off-peak times, for example during the evening. As such, during peak times, where energy costs are most expensive it can be profitable to turn the plant down by decreasing the flow rate of the air that is compressed.
  • The gas flow rate through a compression system can be controlled by an arrangement of inlet guide vanes that can be set from an open position to increasing more closed positions to impart a swirl into the incoming gas and thereby decrease the gas flow rate. More recently, high speed motors have become available that can be directly coupled to a compressor. Such motors also have a speed control that allows the speed of the compressor to be accurately controlled. This control of speed allows the flow rate of the gas to also be controlled in a more thermodynamically efficient manner than with the use of inlet guide vanes. An example of such a motor are permanent magnet motors having a variable frequency drive to control the speed. Such motors can be directly connected to the compressors or each of the compressors in a compression system.
  • There are certain limitations on the use of a speed control to control the flow rate of the gas to be compressed by the compressor. One major limitation concerns undesirable vibration modes within an intended operational speed range for the turbomachine. Since operating on or near these modes can cause rotor displacements that can cause damage to the rotor sufficient to render the motor inoperable, it is common practice to set restricted speed zones and avoid operation on or near these undesirable vibration modes. The width of such zones can render important operation ranges of the motor; and therefore, the compressor unusable.
  • As will be discussed, the present invention provides a method and apparatus for compressing the gas in which desired flow rates of the gas can be safely obtained over the entire operational range of the motor while the overall compressors thermodynamic efficiency is maximized.
  • SUMMARY OF THE INVENTION
  • The present invention may be characterized as a compression train system for an air separation unit comprising: (a) at least one variable speed motor having at least one shaft; (b) at least one air compressor having at least one initial compression stage and adapted to receive and compress a flow of ambient pressure air and to be driven by the at least one shaft of the variable speed motor; and (c) a plurality of downstream compressors or compression turbo-machines disposed in a series arrangement with the at least one initial compression stage. The speed of the variable speed motor is adjusted to increase or decrease the flow rate of the ambient pressure air to the at least one air compressor and the flow rates of the compressed air to the plurality of downstream compressors or compression turbo-machines toward a desired flow rate. Preferably, the speed of the variable speed motor remains situated above or remains situated below a restricted speed zone.
  • The present invention may also be characterized as a method for compressing air, comprising the steps of: (i) receiving a flow of ambient pressure air to at least one air compressor having at least one initial compression stage; (ii) driving the at least one air compressor having at least one initial compression stage with a variable speed motor having at least one shaft; (iii) compressing the flow of ambient pressure air in the at least one air compressor thereby producing a flow of compressed air exiting the at least one air compressor at a first pressure; (iv) further compressing the flow of compressed air at the first pressure to a higher pressure in a plurality of downstream compressors or compression turbo-machines disposed in a series arrangement with the at least one initial compression stage; and (v) adjusting the speed of the variable speed motor to increase or decrease the flow rate of the ambient pressure air to the at least one air compressor and the flow rates of the compressed air to the plurality of downstream compressors or compression turbo-machines toward a desired flow rate.
  • The compression train system and method may include a first centrifugal compressor is mounted on one end of the shaft of the variable speed motor to form a first of the two stages of compression configured to compress the ambient pressure air to a first pressure; and a second centrifugal compressor is mounted on the other end of the shaft and in flow communication with the first centrifugal compressor to form a second of the two stages of compression to further compress the air to a second pressure, higher than the first pressure. Alternatively, the compression train system and method may include a first centrifugal compressor is mounted on one end of the shaft of the variable speed motor to form a first of the two stages of compression and configured to compress a first portion of the ambient pressure air to a first pressure; and a second centrifugal compressor is mounted on the other end of the shaft to form a second of the two stages of compression and configured to compress to also compress a second portion of the ambient pressure air to the first pressure.
  • In still other aspects, the present invention provides a method of producing a compressed gas and controlling flow rate of the compressed gas in which the gas is compressed within a compression system having at least one stage of compression to compress a gas and thereby to produce the compressed gas and an electric motor directly coupled to the at least one stage of compression. The motor has a restricted speed zone within which vibrational modes can damage the compression system. More specifically, the damage to the compression system can be damage to the motor and/or the compressor coupled to the motor. The at least one stage of compression can comprise a centrifugal compressor having inlet guide vanes to control the flow rate of the compressed gas to a desired flow rate and the electric motor can have a speed controller to control the speed of the motor and therefore, an impeller of the centrifugal compressor to also control the flow rate of the compressed gas to the desired flow rate. When the desired flow rate is able to be obtained with the speed of the electric motor situated above or below the restricted speed zone, the flow rate is controlled to achieve the desired flow rate by controlling the speed of the electric motor with the speed controller and with the inlet guide vanes set at a 0° swirl angle. As used herein and in the claims and as would be well known to those skilled in the art, the term “0° swirl angle” when used in connection with the position of the inlet guide vanes means that the vanes are set a wide open position such that the flow out of the inlet guide vanes is parallel to a centerline of the flow which commonly would be the centerline of a pipe feeding the gas to the inlet of the compressor. When the desired flow rate is not able to be obtained without the speed of the electric motor situated within the restricted speed zone, the speed of the electric motor is controlled with the speed controller such that the speed is set at an upper speed, above the restricted speed zone and the inlet guide vanes are set to obtain the desired flow rate.
  • The flow rate of the compressed gas can be measured downstream of the compression system to obtain a measured flow rate. The measured flow rate can be compared with the desired flow rate to obtain an error in the desired flow rate if a difference between the measure flow rate and the desired flow rate exists. When the desired flow rate is able to be obtained with the speed of the electric motor situated above or below the restricted speed zone, the error in the desired flow rate is minimized by adjusting the speed of the electric motor with the speed controller. When the desired flow rate is not able to be obtained without the speed of the electric motor situated within the restricted speed zone, the error in the desired flow rate is minimized by adjusting the inlet guide vanes.
  • When a current speed of the electric motor is situated at the upper speed, above the restricted speed zone and the desired flow rate is currently obtained by adjusting the inlet guide vanes to a current position of the inlet guide vanes and a new speed of the electric motor, below the restricted speed zone, is required to obtain a new desired flow rate, the speed of the electric motor is decreased in decreasing speed steps. At the same time, the inlet guide vanes are successively opened during each of the decreasing speed steps such that the inlet guide vanes are set at the 0° swirl angle at a lower speed, below the restricted speed zone. The speed is thereafter, decreased until the new speed is obtained.
  • When the current speed of the electric motor is situated below the restricted speed zone and the desired flow rate is not able to be obtained without the speed of the electric motor situated within the restricted speed zone, the position of the inlet guide vanes required to obtain the desired flow rate at the upper speed, above the restricted speed zone, is calculated. The speed of the electric motor, with the inlet guide vanes set at the 0° swirl angle, is set at the lower speed, below the restricted speed zone. Thereafter, the speed of the electric motor is increased in increasing speed steps until the upper speed, above the restricted speed zone is obtained. Additionally, the inlet guide vanes are successively closed during each of the increasing speed steps such that the position of the inlet guide vanes required to obtain the desired flow rate will be reached when the upper speed, above the restricted speed zone, is reached. In this regard, as would be well understood by those skilled in the art, the successive closing of the inlet guide vanes would impart more swirl to the flow entering the compressor and therefore, decrease the flow rate to the desired flow rate.
  • The electric motor can be a high speed permanent magnet motor and the speed controller can be a variable frequency drive. In such case, the compression system can have two stages of compression to compress the gas. The centrifugal compressor is a first centrifugal compressor mounted on one end of a motor shaft of the high speed permanent magnet motor to form a first of the two stages of compression and to compress the gas to a first pressure. A second centrifugal compressor, in flow communication with the first centrifugal compressor, is mounted on the other end of the motor shaft to form a second of the two stages of compression to further compress the gas to a second pressure, higher than the first pressure.
  • In an alternative embodiment, the compression system can have two centrifugal compressors having a common feed through which the two centrifugal compressors are fed with the gas and a common outlet from which the compressed gas is discharged. The centrifugal compressor is a first of the two centrifugal compressors mounted on one end of a motor shaft of the high speed permanent magnet motor and a second of the two centrifugal compressors is mounted on the other end of the motor shaft. Each of the first and the second of the two centrifugal compressors have the inlet guide vanes.
  • The present invention also provides an apparatus for producing a compressed gas and controlling flow rate of the compressed gas. The apparatus comprises a compression system having at least one stage of compression to compress a gas and thereby to produce the compressed gas. An electric motor, directly coupled to the at least one stage of compression, has a restricted speed zone within which vibrational modes can damage the compression system. The at least one stage of compression can comprise a centrifugal compressor having inlet guide vanes responsive to an inlet guide vane positioning signal to control the flow rate of the compressed gas to a desired flow rate and the electric motor has a speed controller responsive to a speed control signal to control the speed of the motor and therefore, an impeller of the centrifugal compressor to also control the flow rate of the compressed gas to the desired flow rate.
  • A master controller generates the inlet guide vane signal and the speed control signal. The master controller is programmed to calculate a calculated speed of the electric motor to obtain the desired flow rate and an inlet guide vane position at a speed level at an upper speed, above the restricted speed zone that will obtain the desired flow rate. Additionally, the master controller is also programmed to generate the speed control signal such that the speed control signal is referable to the calculated speed when the calculated speed is situated above or below the restricted speed zone and generate the inlet guide vane positioning signal such that the inlet guide vanes will be set at the 0° swirl angle. When the calculated speed is situated within the restricted speed zone, the master controller is also programmed to generate the speed control signal such that the speed control signal will be referable to the speed level at an upper speed, above the restricted speed zone and the inlet guide vane positioning signal will be referable to the inlet guide vane position that will obtain the desired flow rate.
  • A flow transducer is situated downstream of the compression system and is configured to generate a flow signal referable to the actual flow rate of the compressed gas. The master controller is responsive to the flow signal and is also programmed to compare the actual flow rate with the desired flow rate and generate an error in the desired flow rate if a difference between the actual flow rate and the desired flow rate exists. When the calculated speed is situated above or below the restricted speed zone, the speed signal is generated to minimize the error in the desired flow rate and when the desired flow rate is not able to be obtained without the calculated speed being situated within the restricted speed zone, the inlet guide vane positioning signal is generated to minimize the error in the desired flow rate.
  • The master controller is programmed such that when a current speed of the electric motor is situated at the upper speed, above the restricted speed zone and the desired flow rate is currently obtained by adjusting the inlet guide vanes to a current position of the inlet guide vanes and the calculated speed of the electric motor required to obtain a new desired flow rate is below the restricted speed zone, the speed control signal is successively generated to be referable to successively decreasing speeds of the electric motor in decreasing speed steps until a lower speed, below the restricted speed zone, is obtained. Simultaneously, the inlet guide vane positioning signal is successively generated during each successive generation of the speed control signal to be referable to successively greater openings of the inlet guide vanes such that the inlet guide vanes are set at the 0° swirl angle at a lower speed, below the restricted speed zone. Thereafter, the speed control signal is generated such that the calculated speed is obtained.
  • When the current speed of the electric motor is situated below the restricted speed zone and the desired flow rate is not able to be obtained without the speed of the electric motor situated within the restricted speed zone, the position of the inlet guide vanes required to obtain the desired flow rate at the upper speed, above the restricted speed zone is calculated, the speed control signal is generated to be referable to the lower speed, below the restricted speed zone, the speed control signal is successively generated to be referable to successively increasing speeds of the electric motor in increasing speed steps until the upper speed, above the restricted speed zone is obtained. Simultaneously, the inlet guide vane positioning signal is generated during each of the increasing speed steps to be referable to successively closed positions of the inlet guide vanes such that the position of the inlet guide vanes required to obtain the desired flow rate will be reached when the upper speed, above the restricted speed zone, is reached.
  • The electric motor can be a high speed permanent magnet motor and the speed controller can be a variable frequency drive. In such case, the compression system can have two stages of compression and the centrifugal compressor is a first centrifugal compressor mounted on one end of a motor shaft of the high speed permanent magnet motor to form a first of the two stages of compression. A second centrifugal compressor, in flow communication with the first centrifugal compressor, is mounted on the other end of the motor shaft to form a second of the two stages of compression. In an alternative embodiment, the compression system can have two centrifugal compressors having a common feed through which the two centrifugal compressors are fed with the gas and a common outlet from which the compressed gas is discharged. The centrifugal compressor is a first of the two centrifugal compressors mounted on one end of a motor shaft of the high speed permanent magnet motor and a second of the two centrifugal compressors is mounted on the other end of the motor shaft. Each of the first and the second of the two centrifugal compressors have the inlet guide vanes and each are responsive to the inlet guide vane positioning signal.
  • BRIEF DESCRIPTION OF THE DRAWINGS
  • While the specification concludes with claims distinctly pointing out the subject matter that Applicant regards as his invention, it is believed that the invention will be better understood when taking in connection with the accompanying drawings in which:
  • FIG. 1 is a schematic diagram of a compression system for carrying out a method in accordance with the present invention;
  • FIG. 2 is a graphical representation of speed dependent natural rotor frequencies at first and second bending modes for an electric motor utilized in the compression system of FIG. 1.
  • FIG. 3 is the graphical representation of speed dependent natural rotor frequencies of FIG. 2 with restricted speed zones indicated by shaded areas;
  • FIG. 4 is a compressor map of the compressor used in the first stage of compression of the compression system shown in FIG. 1;
  • FIGS. 5A and 5B are a logic flow diagram of the programming utilized in the master controller of the compression system of FIG. 1;
  • FIG. 6 is a logic flow diagram of the programming utilized in an IGV Positioning Subroutine For Speeds Below The Restricted Speed Zone shown in FIG. 5;
  • FIG. 7 is a logic flow diagram of the programming utilized in a Restricted Speed Zone IGV Positioning Subroutine I shown in FIG. 5;
  • FIG. 8 is a logic flow diagram of the programming utilized in a Restricted Speed Zone IGV Position Subroutine II shown in FIG. 5;
  • FIG. 9 is a logic flow diagram of the programming utilized in a Feedback Subroutine shown in FIGS. 5; and
  • FIG. 10 is an alternative embodiment of a compression system for carrying out a method in accordance with the present invention.
  • DETAILED DESCRIPTION
  • With reference to FIG. 1, a compression system 1 in accordance with the present invention is illustrated. Within compression system 1, a gas by way of a gaseous feed stream 10 is compressed in a first compressor 12 having inlet guide vanes 14 to adjust the flow rate of the gas to be compressed. First compressor 12 constitutes a first stage of compression. After removal of the heat of compression in an intercooler 16, the gas is further compressed in a second compressor 18 to a higher pressure to produce a compressed gas stream 20. First and second compressors 12 and 18 are centrifugal compressors of known design having an inlet, an impeller, a diffuser and a scroll-like volute to discharge the gas after having been compressed.
  • The first and second compressors 12 and 18 are connected to oppose ends of a motor shaft 22 of a motor 24 that drives the impellers of such compressors. Motor 24 can be a high speed permanent magnet motor. The speed of permanent magnet motor 24 is controlled by a variable frequency drive 26 that can adjust the speed of the motor 24 and therefore, also the flow rate of the compressed gas stream 20. Variable frequency drive 26 is linked to the motor 24 by an electrical connection 28. The variable frequency drive 26 is responsive to a speed control signal referable to a motor speed that is generated in a master controller 30 and transmitted to the variable frequency drive by an electrical connection 32. In addition to the foregoing, electrical connections 28 and 32 are provided between the motor 24, the variable frequency drive 28, and the master controller 30 to transmit a signal referable to the speed of the motor 24 to in effect allow the programming employed in master controller 30 to measure the actual speed of the motor 24. In case of a motor employing magnetic bearings, sensors related to such bearings would be capable of sending such a signal and is conventional. The master controller 30 also generates an inlet guide vane position signal that is transmitted to a positioner incorporated into the inlet guide vanes 14 by means of an electrical connection 34. The positioner also generates a signal proportional to the position of the inlet guide vanes that is fed back to the master controller 30 to enable the programming logic employed in the master controller 30 to in effect measure the position of the inlet guide vanes 14. The positioner and the inlet guide vanes 14 and its features discussed above are conventional and well known in the art. The master controller 30 is responsive to a flow request 36 for the compressed gas stream 20 that serves as an input 38 to the master controller 30.
  • As will be discussed, motor 24 has a restricted speed zone in which operation can only be conducted for a brief period of time without vibrational modes occurring that can damage the motor and/or the first and second compressors 12 and 18. When a desired flow rate is able to be obtained by speed control without the speed of motor 24 residing within the restricted speed zone, master controller 30 generates a speed control signal in response to the flow request 36 that will produce a speed within the motor 24 that will in turn produce the desired flow rate of the compressed gas stream 20. At such time, the inlet guide vane signal is generated by the master controller 30 to fully open the inlet guide vanes 14 or in other words, set the inlet guide vanes 14 to the 0° swirl position. When the desired flow rate is not able to be obtained without the speed of the motor 24 being within the restricted speed zone, the speed signal is generated by the master controller 30 to set the speed of the motor 24 to the upper speed, above the restricted speed zone and the inlet guide vane signal is generated to close the inlet guide vanes to produce the desired flow rate or in other words, impart more swirl to the incoming flow to the first compressor 12 and thereby decrease the flow rate to the desired flow rate.
  • Optionally, feedback can be provided by a flow transducer 40 that generates a flow signal, referable to the flow of the compressed gas stream 20, that is inputted into the master controller 30 by an electrical connection 42 should there be a difference between the measured flow rate and the flow request 36. In response to the flow signal, the master controller 30 either further adjusts the speed of the permanent magnet motor 24 or the inlet guide vanes 14 or both to minimize the error.
  • It is to be noted that although the present invention is described with reference to a high speed permanent magnet motor, it would have equal applicability to other high speed motors controlled by a variable frequency drive such as an induction motor and a switched reluctance motor. Further, although two compression stages are illustrated in FIG. 1, the present invention would have equal applicability to a single compression stage provided by a compressor connected to the shaft of an electric motor.
  • In an electric motor that is directly coupled to a centrifugal compressor either at one end of a motor shaft or where two centrifugal compressors are directly coupled to opposite ends of the rotor shaft, there are speed dependent natural frequencies for first and second bending motor shaft modes in which extended operation at such speed can damage the electric motor. As shown in FIG. 2, the bending modes have both forward and backward precession modes “F” and “B”. The first bending mode has two nodes (shown by the triangles) that are typically located near the journal bearings supporting the motor shaft 22 for rotation. The second bending mode has three nodes, with the outer two nodes being typically located near such journal bearings and a central node located between the two outer nodes and between the two bearings. Excitation of the forward modes is most commonly created by rotor unbalance and non linear stiffness effects in the bearings, also known as cross coupling. Excitation of the backward modes is most commonly created by the motor shaft rubbing stationary parts such as shaft seals. Due to the ever presence of unbalance and cavity cross coupling of the forward mode, as compared with a typically brief rub event of the backward mode, greater concern is typically given to the forward processing modes while the backward modes are, in many situations ignored or discounted. Therefore, excitation amplitudes for forward modes are more prone to grow to unacceptable levels when compared to the brief rubs exciting the backward modes and can present more of an operational concern.
  • For example, in motor 24, a rotor containing permanent magnets is suspended for rotation by journal bearings that can be magnetic type bearings and which are provided within a motor casing. It is to be noted that hydrodynamic and airfoil type bearings are also possible. A thrust bearing, that can also can be a magnetic or also, possibly a hydrodynamic or airfoil type of bearing, is provided to absorb axial loadings. The first and second compressors 12 and 18 are connected to the motor housing of the permanent magnet motor 24 and, as indicated above, the motor shaft 22 drives two impellers located in the first and second compressors 12 and 18 situated at opposite ends of the motor shaft 22. This collection of rotating parts is referred to as the rotor. In a forward bending mode, as the shaft starts to vibrate and precess in the direction of rotation, the rotor can contact the internal stationary parts within the motor casing resulting in potential damage or destruction of the motor.
  • With reference to FIG. 3, separation margins are placed on the rotor natural frequencies shown in FIG. 1. For purposes of illustrating the use of a separation margin on each rotor bending mode in both forward and backward precession directions, representative, yet arbitrary values of separation margin for each mode are listed in FIG. 3 next to the abbreviation SM. The actual separation margins used are typically a function of the amount of damping present as well as experience or industrial guidelines. For instance, the American Petroleum Institute provides such guidelines in its publication API 684. It is to be noted that the rotor natural frequencies shown in this illustration are a product of analytical calculations made during the design phase of the motor. Consequently, these are predicted dynamic responses that have a degree of uncertainty. Moreover, even the same motors will have slight differences due to the tolerances involved in fabricating such motors that also will present a degree of uncertainty. The separation margins therefore represent tolerances in such lines that are present for the safe operation of the motor. The shaded area enclosed by these lines are thus, restricted speed zones for the motor where operation, while not prohibited, is restricted to brief time intervals to prevent excitation of bending modes that are possible within such zones from producing damage to the motor.
  • The diagonal line is referred to as an operating line that has a slope of 1 to conveniently ascertain the bounds of such restricted speed zones. It is to be noted that the rotor natural frequency plots in FIGS. 1 and 2 are exemplary only and such plots will vary in different motors. Furthermore, for purposes of example, it is assumed that there exists sufficient damping provided by the bearings such that the backward precession mode of the first bending mode can be ignored. However, the backward precession mode in the second bending mode is to be avoided. However, as mentioned above, this is of less concern and therefore, the safety margin is often selected to be less than the forward precession mode of the first bending mode. It is further assumed that for purposes of example that the motor need only operate at 9000 rpms. Since this is at the lower limit of the safety margin of the backward precession mode of the second bending mode, this motor speed will represent an upper limit of operation. However, if the motor did require operation at higher speeds there could be three restricted speed zones, namely both the forward precession mode of the first bending mode, the backward precession mode of the second bending mode and the forward precession mode of the second bending mode. In this example, however, there is one restricted speed zone and the same would lie between, but would not include, 6300 and 6800 rpms. Given that the proposed operation of the motor is between 5000 and 9000 rpms, this restricted speed zone represents 12.5 percent of the operational speed range of the motor that would be unavailable for regulating the flow rate of one or more compressors connected to the motor. With reference to FIG. 4, a compressor map is shown for the compressor 12. As indicated the compressor is capable of delivering a flow rate from between 12 and 30 LBM/Sec (pound mass per second) of flow over the operating speed range. The restricted speed zone prevents delivery of mass flows from 19 LBM/Sec to 21 LBM/Sec or in other words about 17 percent of the range of flow rates to be delivered by manipulation of speed alone.
  • With reference to FIGS. 5A and 5B, the master controller 30 is programmed with a control program, with specific reference to FIG. 5A, the control program begins execution at the execution stage 50 “Begin” with the input a new flow rate “QS” specified in execution stage 52 through input of a flow request 36 as illustrated in FIG. 1. The current flow rate “QR” is measured by flow transducer 40 and is input into execution stage 54 along with the current speed of the NR that is preferably stored as data within the controller 30. A flag, “Feedback” is set to “off” in stage 55 and the program then proceeds to execution stage 56 in which data contained in a compressor map of the type illustrated in FIG. 4 is obtained to determine the speed of the compressor with the inlet guide vanes 14 set at 0°. This speed is referred to by the variable NS.
  • The program then proceeds to execution stage 58 to perform a test to determine whether the new speed, “NS” is outside the minimum or maximum speed of the first compressor 12. In the Example discussed above, the minimum and maximum speed of the compressor would be in a range from 5000 and 9000 rpms. If the answer to the test is yes, then execution stage 60 executes and a message is sent to the operator that the requested flow rate is out of range.
  • If the answer to the test is no, then execution stage 62 executes in which a test is performed to determine whether the new speed is in the restricted speed zone which in the example given above would be between 6300 and 6800 rpms. If the answer to the test is no, then execution stage 64 executes in which a further test is performed to determine whether the current speed NR is at an upper speed, above the restricted speed zone. In the example, the upper speed would be 6800 rpms since the restricted speed zone lies below this speed. It is to be noted, that such upper speed could be set higher than 6800 rpms, for instance 7000 rpms to provide even a greater margin than that calculated for the specific motor. If the answer to the test is no, then a speed signal is generated by the master controller 30 which, as indicated in execution stage 66 is sent via electrical connection 32 to the variable frequency drive 26 to in turn set the motor 24 to the speed referable to the speed signal. The program then proceeds to a “Feedback Subroutine” 68 and then to the end of program execution as designated by reference number 70. Prior to executing the Feedback Subroutine 68, two variables “IGV” and “IGVS” are both set to 0 as shown at 67 and 71, respectively. The setting of the current position of the inlet guide vanes 14 “IGV” and the specified position thereof “IGVS” at 0 is necessary to allow the Feedback Subroutine 68 to properly execute and define a new reference inlet guide vane position “IGVR” to be equal to 0. The Feedback Subroutine 68 allows the speed of the motor 24 or the position of inlet guide vanes 14 to be adjusted as required to obtain the new flow rate QS should the measured flow rate that is obtained not be equal to QS. However, it is to be noted that embodiments of the present invention in which there is no such feedback control are possible and therefore, Feedback Subroutine 68 is optional.
  • If the test in execution stage 64 is yes, then another test is performed in execution stage 72. If as indicated in execution stage 72, the test produces a negative answer, then only the speed of the motor 24 need be adjusted with a 0° swirl angle of the inlet guide vanes 14, in other words, fully open, to obtain the desired flow rate of the compressed gas stream 20. Reviewing the logic, as indicated in execution stage 62, the new speed is not in the restricted speed zone, the current speed is in a restricted speed zone as tested in execution stage 64 and since the new speed as tested in the execution stage 72 is not below the restricted speed zone, the new speed must be above the restricted speed zone. As such, in order to produce the desired flow rate, as indicated in execution stage 74, an inlet guide vane positioning signal is generated to reposition the inlet guide vanes 14 to the 0° swirl angle so that no swirl is generated and a speed control signal is generated that is referable to the desired speed that will obtain the desired flow rate. These signals are transmitted to the variable frequency drive 26 and to the inlet guide vanes 14 by electrical conductors 32 and 34, respectively. Since the positioning of the inlet guide vanes 14 is not instantaneous, a loop is performed in which a signal referable to the inlet guide vane position is transmitted from inlet guide vanes 14 back to the master controller through electrical connection 34 to measure the current position of the inlet guide vanes 14 as indicated in execution stage 76. Thereafter a test is performed as shown in execution stage 78 in which the measured inlet guide vanes position is tested against the 0° desired position. If the answer to the test is no, the execution of the control program loops back to execution stage 76 until the desire position IGVM of 0° is reached or in other words, until the test performed in execution stage 78 can be answered in the affirmative. Thereafter, the program executes a loop in which the speed “N” of the motor 24 is measured at 79 and the speed is then tested in stage 80 to determine whether the measured speed has reached NS, the specified speed. If the motor 24 has not reached the specified speed, the program loops back to 79 until the measured speed has in fact reached the specified speed. At such time, the variable “IGVS” is set to 0 and the programming proceeds to the Feedback Subroutine 68 and then the program end 70. The setting of the variable “IGVS” to 0 supplies a necessary variable to the Feedback Subroutine 68 to allow it to properly execute.
  • Turning back to execution stage 72, if the answer to the test is in the affirmative, then the desired flow rate will be obtained at a speed of motor 24 below the restricted speed zone. While it is possible to immediately set the inlet guide vanes to a 0° position for such purposes, this may be undesirable because the speed of motor would at such time be at the uppermost level of the restricted speed zone and the flow would increase rather than decrease because at such time, the inlet guide vanes 14 are controlling the flow rate. In most applications of the present invention, it is more preferable that movement of the inlet guide vanes 14 be gradual with flow decreasing monotonically. With specific reference to FIG. 5B, in order to gradually move the inlet guide vanes 14, after an affirmative outcome of the test of execution stage 72, an IGV Positioning Subroutine for Speed Below the Restricted Speed Zone 82 executes. In the Subroutine 82, both the speed of the motor 24 is incrementally decreased while within the restricted speed zone and the inlet guide vanes 14 are incrementally opened to the 0° swirl angle. The speed of the motor is also adjusted to obtain the desired flow rate QS.
  • With reference to FIG. 6, the subroutine generally shown at 82 initiates with a lookup of the upper Speed NU, above the restricted speed zone and then a look up of the lower speed NL, below the restricted speed zone as indicated at 83 and 84, respectively. This “lookup” can be performed by simply reading data referable to these values, namely, 6300 and 6800 rpms. The user is able to select the number of steps that the speed will be dropped or these may be pre-programmed. In any case, assuming a user selected speed step, the same will be an input into the control program of the master controller 30 and will have a value of “K”. As indicated at 86, the program then performs a calculation to determine the incremental speed drop for the motor 24 by subtracting the lower speed, below the restricted speed zone “NL” from the upper speed, above the restricted speed zone “NU” and dividing the difference by the number of steps “K” that the user has selected. Thus, assuming 10 steps were selected by a user, then the speed will be adjusted in decreasing steps of 50 rpms. The position of the vanes “IGVC” of the inlet guide vanes 14 is then measured by transmitting the value from the inlet guide vanes 14 to the master controller 30 as shown at 88. In the next execution stage an incremented speed Ni is sent to the motor 24 by means of a speed signal referable thereto generated by the programming in the master controller 30 and sent to the variable frequency drive 26 as indicated in execution stage 90. For example, assuming that the speed is at the upper speed level of 6800 rpms and ten fifty rpm steps have been selected, the first increment Ni is set equal to 6750 rpms. Thereafter, the required position of the inlet guide vanes is calculated at execution stage 92. This is simply a ratio of the difference between the current incremental speed value Ni and NL to the speed range of the restricted speed zone, namely Nu-NL. This ratio is multiplied by the current position of the inlet guide vanes 14 determined at execution stage 88 above. Consequently, as Ni approaches NL, the position of the inlet guide vanes 14 will approach 0° swirl angle and thus, be fully opened. The results of execution stage 92 are then fed into execution stage 94 in which the inlet guide vane positioning signal value is either looked up or computed to obtain the value calculated in execution stage 92. Such signal, as indicated in execution stage 96 is then transmitted to the inlet guide vanes 14 from the master controller 30 over the electrical connection 34.
  • Since the reaction of motor 24 to a speed change is not instantaneous, the speed of the motor 24 is measured at 98. Further, since the positioning of the inlet guide vanes is also not instantaneous, the program loops between a step in the programming 100 in which the position of the vanes in the inlet guide vanes 14 is measured by transmittal to the master controller 30 and then a test is performed at 102 to determine whether the inlet guide vanes 14 are at the position calculated at execution stage 92 of the programming. If the result of the test of 102 is negative, then execution stage 100 is re-executed until the test is positive. At such time, a further test is performed in execution stage 104 to determine whether the speed of the motor 24, that is obtained in execution stage 98, has reached the incremented speed Ni. If the answer is in the negative, the programming loops back to execution stage 98. If the test of 104 is positive, or the measured speed has reached the incremented speed, then as set forth in execution stage 106, the speed is tested to determine whether the speed measured in stage 98 has reached the lower speed, below the restricted speed zone NL. If the answer to such test is no, then the speed is incremented to a new value of Ni as indicated in execution stage 108. For instance, if the speed is presently at 6750 rpms, then the next increment in a user specified 10 step routine would be 6700 rpms, assuming a 50 rpm increment. The program would then loop back to execution stage 90 to set the new increment in the speed to the motor 24. If, however, the answer to the test of execution stage 106 is in the affirmative, the inlet guide vanes 14 are set in the fully open position and at the 0° swirl angle. In stage 109 of the programming, a speed signal is generated that will send the required speed to produce the desired flow, as determined in execution stage 56, to the variable frequency drive 26 to set the motor 24 at such speed. The programming will then proceed to a loop in which the speed is measured in stage 110 and then tested in 111 to determined whether the measured speed has reached the specified speed NS. When the test is in the positive, the variable IGVS is set equal to IGV as indicated in step 112 and the programming proceeds to the Feedback Subroutine 68 and program end 70. The setting of “IGVS” to be equal to “IGV” allows the Feedback Subroutine 68 to properly execute.
  • With reference again to FIG. 5A and to execution stage 62, assuming the answer to the test is yes because the new speed is in a restricted speed zone, execution stage 113 is next executed as shown in FIG. 5B. Execution stage 113 tests whether the current speed is at the upper speed NU, above the restricted speed zone. Assuming it is not and therefore, the answer to the test is no, then the current speed can either be above or below the restricted speed zone. This is determined in execution stage 114 and assuming that the answer to the test is no, then, the Restricted Speed Zone IGV Positioning Subroutine I is executed as set forth at 115. In this subroutine, the speed of motor 24 will be set at the upper speed above the restricted speed zone and the desired flow rate will be obtained with the inlet guide vanes 14 to impart the requisite swirl to the flow.
  • With additional reference to FIG. 7, the logic employed in the programming of the subroutine of 115 begins at execution stage 116 with a lookup of the upper speed “NU”, above the restricted speed zone which in the example is 6800 rpms. Again, for purposes that will be discussed, the specified speed variable NS is set to NU at 117. A speed signal is then generated by the master controller 30 which is transmitted to the variable speed drive 26 and the motor 24 is set to operate at such speed as set forth in execution stage 118. Since the speed was above the upper speed, above the restricted speed zone, the motor 24 must decelerate. As such a loop is executed in which the speed of the motor 24 is measured at 120 and then a test is performed in execution stage 122 to determine whether the motor 24 has reached the upper speed above the restricted speed zone. When the answer to the test is yes, the programming proceeds to 124 where a lookup is performed in a lookup table to determined the position of vanes in inlet guide vanes 14 to obtain the new flow rate that has been requested as set forth at reference number 36 in FIG. 1 and in particular, the execution stage 52 of the programming. With reference again to FIG. 4, the dashed lines represent possible swirl angle positions of the inlet guide vanes 14 to obtain the desired flow rates at a speed set at the upper limit of the restricted speed zone. The position selected would be at the intersection of the dashed lines with the system resistance line at which pressure ratios and mass flow are obtained at specific compressor speeds. In this particular compressor vane positions of between 0° and 20° would be available to obtain the desired flow rates within the restricted speed zone. Data concerning the vane positions and mass flow would be stored in the look up table and points between actual stored data could be interpolated.
  • Following execution stage 124, either by means of a lookup table or computation an inlet guide vane positioning signal is computed for the inlet guide vanes 14 at 126 and the signal is then sent to the inlet guide vanes 14 at 128 from the master controller 30. Since the positioning of the inlet guide vanes 14 is not instantaneous, a loop is performed in which the position of the vanes within the inlet guide vanes 14 is measured at 130 and a test is performed at 132 to determine whether the inlet guide vanes 14 are at the position to obtain the desired flow rate. When the answer to the test is yes, then the programming proceeds to the feed back subroutine 68 and then to end 70.
  • With reference to FIG. 5B, assuming that the test performed in execution stage 114 is in the affirmative or in other words, the current speed is below the restricted speed zone, the programming contained in the Restricted Speed Zone IGV Positioning Subroutine II 134 is executed. In this subroutine, the speed of the motor is increased to the lower speed below the restricted speed zone and then the speed is incrementally increased until the upper speed above the restricted speed zone is reached. During each increment in the speed, the inlet guide vanes 114 are incrementally closed until a position is reached at which the desired flow rate will be obtained with the speed of the motor 24 at the upper speed, above the restricted speed zone.
  • Specifically, with additional reference to FIG. 8, the subroutine 134 is programmed so that first the lower speed, below the restricted speed zone “NL” is determined in execution stage 136. A speed signal referable to the lower speed “NL” is then generated by the master controller 30 and transmitted to the variable frequency drive 26 to adjust the speed of the motor 24 to such speed as indicated in execution stage 138. Since the acceleration of the motor 24 is not instantaneous, a loop is then performed in which the speed of the motor 24 is measured at 142 and then tested in execution stage 143 to determine whether the motor speed has reached the lower speed, below the restricted speed zone. When the answer is in the affirmative, then a lookup in a lookup table is performed in execution stage 144 to determine the positioning of the inlet guide vanes 14 to obtained the desired flow rate of the compressed gas stream 20 at the upper speed, above the restricted speed zone by means of the use of data of the type mentioned above with respect to FIG. 4. For purposes that will be discussed the variable “NS” is set to the upper speed variable “NU” at 145. Thereafter, in execution stage 146, the user, as in input to the master controller 30 can specify a number of steps “K” to increment the speed to raise the speed of the motor 24 from the lower speed, below the restricted speed zone to the upper speed, above the restricted speed zone. This speed increment is given by the difference between the uppermost and lower speeds divided by the increment. For instance, in the example above, if ten increments were desired, then the speed increment would be 50 rpms. For example, assuming that the speed is at the lower level of 6300 rpm and ten fifty rpm steps have been selected, first speed increment “NI” is set equal to 6350 rpm.
  • In the next stage of execution designated by reference number 148, a speed signal is generated referable to the incremented speed, “Ni” that is generated by the master controller 30 and transmitted to the variable frequency drive 26 to set the motor to the incremented speed. The position of the inlet guide vanes 14 is also incremented by a ratio multiplied by the required inlet guide vane position “IGVS” of the inlet guide vanes 14 in execution stage 150. This ratio is between a difference between the current value of Ni and the lower speed level of the restricted speed zone (Ni—NL) divided by the difference between the uppermost and lower speeds of the restricted speed zone (NU-NL). When the incremented speed is equal to NU, obviously the ratio will be equal to 1 and the inlet guide vane position will be equal to IGVS. The incremental value of the inlet guide vane position IGVi determined at 150 is then used to lookup or compute an inlet guide vane positioning signal in execution stage 152 that will be generated by master controller 30. This signal is sent to inlet guide vanes 14 in execution stage 154 to incrementally close the inlet guide vanes 14.
  • The programming then executes a loop in which the speed of the motor 24 and position of the inlet guide vanes 14 are measured in 156 and 158, respectively. Then a test is performed in execution stage 160 to determine whether the measured position of the inlet guide vanes 14 has reached the value calculated in execution stage 150. When the answer to this test is yes, then the measured speed N is compared to the incremented speed Ni at 162. If the answer to the test is in the negative, the programming loops back to 156. If the answer to the test of 160 is in the affirmative, then a test is performed at 164 to determine whether the measured speed has reached the upper speed above the restricted speed zone “NU”. If the test performed in execution stage 164 is negative, then the speed is incremented to a new value of Ni at 166 and the programming loops back to execution stage 148 to set the motor 24 to operate at the incremented speed. When the answer to the test of 164 is “yes” in that speed has in fact reached the upper limit of the restricted speed zone, for purposes of proper execution of the Feedback Subroutine 68, the variable “IGVs” is set equal to “IGV” at 168. The Feedback Subroutine 68 is then executed and the programming will then proceed to end at 70.
  • Referring back to FIG. 5B and to execution stage 113, if the current speed is at the upper speed, above the restricted speed zone, a lookup is performed at 170 to determine “NU”, the upper speed, above the restricted speed zone. The variable NS is set equal to NU at 172 and the flag “Feedback” is tested at 174 as to whether it is set “Off”. If the answer to this question is yes, as would be the case if the feed back subroutine were not reached directly before the time of such test, a lookup is performed at 176 in a lookup table to determine the required position of the inlet guide vanes 14 in a manner discussed above with respect to the type of data shown in FIG. 4. Thereafter, in execution stage 178, the required inlet guide vane positioning signal is either determined from a lookup table or computed. The inlet guide vane positioning signal is then generated by master controller 30 and sent to inlet guide vanes 14 in execution stage 180. A loop is then executed wherein the position of the inlet guide vanes 14 is measured at 182 and a test is performed to determine whether the measured value has reached the required position of the inlet guide vanes at 184. When the answer to the test is yes, the programming proceeds to the feed back subroutine 68 and then the program end 70.
  • It is to be noted that in the subroutines and programming discussed above, the inlet guide vanes 14 are being opened in a ratio related to the current incremented speed. It is possible, however, that such incremental opening could be by a fixed percentage and the speed could be incremented by a fixed percentage. However, as can be appreciated, if this were done, then either required speed would be reached before the required inlet guide vane opening or vice-versa. In such case programming would also have to be provided to obtain the required speed or inlet guide vane opening in a percentage that completed the speed or required opening. Such final percentage would differ from the fixed percentage. At the other extreme it is also possible to simply open the inlet guide vanes to the 0° position while sending a speed command to the motor 24 at which the motor will runs at the speed Ns that will produce the desired flow rate.
  • With reference to FIG. 9, feed back control may be executed by the Feedback Subroutine 68 to make certain that the measured flow rate “Q” has in fact reached the specified flow rate “QS”. It is to be noted that an embodiment of the present invention is possible that does not use such feed back control and would depend on calculated values for control of flow rate. However, assuming such feed back control is employed, as indicated, the flow rate is measured at 186 by such means as the flow transducer illustrated in FIG. 1 and a test is performed at 188 to determine whether the “Q” is equal to “QS”. If this has in fact occurred, then the programming proceeds to end 70 and no feed back control is required. Assuming that the test of 188 is “no”, then the flag “Feedback” is set to “on” at 190. Thereafter, as indicated at 192, an updated, new specified speed NNS is calculated. This calculation is performed in execution stage 194. In this calculation, the current value of NS, the specified speed of the motor 24, is increased or decreased by a ratio of a difference between the specified and measured flow rates (QS-Q)and a difference between the measured flow rate and the reference flow rate (Q-QR) that is in turn multiplied by a difference between the current value of the specified speed and the reference speed (NS-NR). The value of NS is then redefined as NNS as shown in execution stage 196.
  • After the calculation of the new specified speed, a calculation is performed for new specified IGV position, “IGVNS” as shown at 198. As indicated at 200, IGVNS is the current specified value of the inlet guide vanes 14, or IGVS either increased or decreased by the same ratio of flow rates used in the calculation of the new specified speed multiplied by a difference between IGVS and IGVR. The new specified position of the inlet guide vanes 14 is then redefined in execution stage 202. It is to be noted that if the programming has proceeded from execution stages 67 and 71 or from execution stage 81 or from subroutine 82, then IGVNS will remain at 0 or in other words, the 0° swirl angle. If the programming has proceeded from subroutines 115 and 134 or execution stage 184, the value of IGVS will be that value defined in such subroutines or execution stage 184.
  • After the computation of the new specified speed of the motor 24 and the new specified position of the inlet guide vanes 14, as shown in execution stage 204, a new reference speed, reference flow rate and reference IGV position are defined by the current measured speed of the motor 24, the current measured flow rate and the current measured position of the inlet guide vanes 14. The programming than loops back to execution stage 58.
  • Assuming that the values of NS and NR are not in a restricted speed zone, the speed of the motor 24 will be adjusted in execution stage 66, subsequent to the feed back subroutine 68 by either increasing or decreasing the speed of the motor until Q is equal to QS. In other words, the speed in such case is adjusted to minimize the error in the flow. Another possibility is that NS will be in the restricted speed zone and the current speed of the motor will be at the upper speed level NU, above the restricted speed zone. In such case, the answer to the test of execution stage 113 would be “yes”. However, the flag “feedback” would be set to “on”. In such case, execution stage 176 would be by-passed as the answer to the test of execution stage 142 would be yes, and the value of IGVS to be sent to the inlet guide vanes 14 would be IGVNS developed in execution stage 200 of the feed back subroutine 68. Thus, the flow rate error would be minimized by adjusting the inlet guide vanes 14.
  • With reference to FIG. 10, it is understood that the present invention has applicability to a compression system 1′ in which the compressed air stream 10 is introduced into two compressors 12 a and 12 b from dual feeds 206 to produce a compressed gas stream 20′ from dual outlets 208. The compressors 12 a and 12 b are mounted on the ends of the motor shaft 22 of the motor 24 and are provided with inlet guide vanes 14 a and 14 b that are controlled through electrical connections 34 a and 34 b that transmit inlet guide vane positioning signals thereto from the master controller 30. Electrical connections 34 a and 34 b also transmit signals from the inlet guide vanes 14 a and 14 b back to the master controller 30 to indicate the position of vanes within the inlet guide vanes 14 a and 14 b. The programming to control the speed of motor 24 and the position of vanes within inlet guide vanes 14 a and 14 b could be the same as outlined above with respect to the compression system 1 discussed above with identical inlet guide vane positioning signals sent to inlet guide vanes 14 a and 14 b and with the programming reacting to the position of the vanes of one of the inlet guide vanes 14 a and 14 b since the same would be identical units. Furthermore, the speed signal would be generated in an identical manner to control the speed of motor 24 to that outlined above with such speed set at the uppermost limit of the restricted speed zone where a flow request were generated that would otherwise require a motor speed within the restricted speed zone and with the flow rate adjusted by the inlet guide vanes 14 a and 14 b.
  • As is apparent from the above discussion; and FIG. 4 in particular, a byproduct of increasing or decreasing flow with a simple speed increase or decrease is accompanied by an increase or decrease in the pressure ratio, respectively. Since many industrial applications involve multiple compression turbomachines in a series arrangement (also known as a compression train), and benefit from or need for both control over flow as well as overall train pressure ratio, it is possible to employ the present invention in such a compression train in the initial stages or stages of compression. Pressure would be recovered in subsequent stages by an increase of the speed of the downstream stages. It is also possible to employ the present invention as illustrated in an application where the flow rate oscillates about the restricted speed zone and therefore, there are no major pressure excursions and where such pressure excursions are able to be tolerated in such application.
  • While the present invention has been described with reference to preferred embodiments, as would occur to those skilled in the art, numerous changes and omissions thereof could be made without departing from the spirit and scope of the present invention as set forth in the appended claims.

Claims (24)

1. A compression train system for an air separation unit comprising:
at least one variable speed motor having at least one shaft;
at least one air compressor having at least one initial compression stage and adapted to receive and compress a flow of ambient pressure air and to be driven by the at least one shaft of the variable speed motor; and
a plurality of downstream compressors or compression turbo-machines disposed in a series arrangement with the at least one initial compression stage;
wherein the speed of the variable speed motor is adjusted to increase or decrease the flow rate of the ambient pressure air to the at least one air compressor and the flow rates of the compressed air to the plurality of downstream compressors or compression turbo-machines toward a desired flow rate.
2. The compression train system of claim 1, wherein the speed of the variable speed motor remains situated above or remains situated below a restricted speed zone.
3. The compression train system of claim 2, further comprising inlet guide vanes disposed on the at least one air compressor and wherein the flow rate of the ambient pressure air to the at least one air compressor is further adjusted by adjusting inlet guide vanes to avoid the speed of the variable speed motor being situated within the restricted speed zone.
4. The compression train system of claim 1, wherein the at least one initial compression stage further comprises two compression stages and wherein the two compression stages are driven by the variable speed motor.
5. The compression train system of claim 4, further comprising:
a first centrifugal compressor is mounted on one end of the shaft of the variable speed motor to form a first of the two stages of compression configured to compress the ambient pressure air to a first pressure; and
a second centrifugal compressor is mounted on the other end of the shaft and in flow communication with the first centrifugal compressor to form a second of the two stages of compression to further compress the air to a second pressure, higher than the first pressure.
6. The compression train system of claim 4, further comprising:
a first centrifugal compressor is mounted on one end of the shaft of the variable speed motor to form a first of the two stages of compression and configured to compress a first portion of the ambient pressure air to a first pressure; and
a second centrifugal compressor is mounted on the other end of the shaft to form a second of the two stages of compression and configured to compress to also compress a second portion of the ambient pressure air to the first pressure.
7. The compression train system of claim 6, further comprising a common feed through which the first centrifugal compressor and the second centrifugal compressor are fed with the ambient pressure air.
8. The compression train system of claim 6, further comprising a common outlet from which the compressed air is discharged from the first centrifugal compressor and the second centrifugal compressor.
9. The compression train system of claim 6, wherein the speed of the variable speed motor remains situated above or remains situated below a restricted speed zone.
10. The compression train system of claim 6, further comprising inlet guide vanes disposed on the at least one air compressor and wherein the flow rate of the ambient pressure air to the at least one air compressor is further adjusted by adjusting inlet guide vanes to avoid the speed of the variable speed motor being situated within the restricted speed zone.
11. A method for compressing air, comprising the steps of:
receiving a flow of ambient pressure air to at least one air compressor having at least one initial compression stage;
driving the at least one air compressor having at least one initial compression stage with a variable speed motor having at least one shaft;
compressing the flow of ambient pressure air in the at least one air compressor thereby producing a flow of compressed air exiting the at least one air compressor at a first pressure;
further compressing the flow of compressed air at the first pressure to a higher pressure in a plurality of downstream compressors or compression turbo-machines disposed in a series arrangement with the at least one initial compression stage;
adjusting the speed of the variable speed motor to increase or decrease the flow rate of the ambient pressure air to the at least one air compressor and the flow rates of the compressed air to the plurality of downstream compressors or compression turbo-machines toward a desired flow rate.
12. The method of claim 11, wherein the step of adjusting the speed of the variable speed motor to increase or decrease the flow rates further comprises adjusting the speed of the variable speed motor while maintaining the speed of the variable speed motor above or below a restricted speed zone.
13. The method of claim 12, wherein the at least one air compressor includes inlet guide vanes and the step of adjusting the speed of the variable speed motor to increase or decrease the flow rates further comprises adjusting the inlet guide vanes to avoid the speed of the variable speed motor being situated within the restricted speed zone.
14. The method of claim 11, wherein the at least one initial compression stage further comprises two compression stages and wherein the two compression stages are driven by the variable speed motor.
15. The method of claim 14, wherein a first centrifugal compressor is mounted on one end of the shaft of the variable speed motor to form a first of the two stages of compression and a second centrifugal compressor is mounted on the other end of the shaft to form a second of the two stages of compression, and wherein the step of compressing the flow of ambient pressure air further comprises the steps of:
compressing the flow of ambient pressure air in the first centrifugal compressor to the first pressure; and
further compressing the air from the first centrifugal compressor at the first pressure to a second pressure, higher than the first pressure in the second centrifugal compressor.
16. The method of claim 14, wherein a first centrifugal compressor is mounted on one end of the shaft of the variable speed motor to form a first of the two stages of compression and a second centrifugal compressor is mounted on the other end of the shaft to form a second of the two stages of compression, and wherein the step of compressing the flow of ambient pressure air further comprises the steps of:
compressing a first portion of the flow of ambient pressure air in the first centrifugal compressor to the first pressure; and
compressing a second portion of the flow of ambient pressure air in the second centrifugal compressor to the first pressure.
17. The method of claim 16, wherein the first centrifugal compressor and the second centrifugal compressor are fed with the ambient pressure air from a common feed and the step of receiving a flow of ambient pressure air further comprises receiving a flow of ambient pressure air from the common feed to the first centrifugal compressor and the second centrifugal compressor.
18. The method of claim 16, wherein the first centrifugal compressor and the second centrifugal compressor are discharged at the first pressure to a common outlet and the method further comprises the step of discharging the flow of compressed air exiting the first centrifugal compressor and the second centrifugal compressor to the common outlet.
19. The method of claim 16, wherein the step of adjusting the speed of the variable speed motor to increase or decrease the flow rates further comprises adjusting the speed of the variable speed motor while maintaining the speed of the variable speed motor above or below a restricted speed zone.
20. The method of claim 19, wherein the first centrifugal compressor and the second centrifugal compressor each have inlet guide vanes and the step of adjusting the speed of the variable speed motor to increase or decrease the flow rates further comprises adjusting the inlet guide vanes to avoid the speed of the variable speed motor being situated within the restricted speed zone.
21. The method of claim 11, wherein the at least one air compressor includes inlet guide vanes and wherein, when the desired flow rate is able to be obtained with the speed of the variable speed motor situated above or below the restricted speed zone, the flow rate of the ambient pressure air to the at least one air compressor is controlled by adjusting the speed of the variable speed motor with a speed controller and with the inlet guide vanes set at a 0° swirl angle.
22. The method of claim 21, wherein, when the desired flow rate is not able to be obtained without the speed of the variable speed motor situated within the restricted speed zone, the flow rate of the ambient pressure air to the at least one air compressor is controlled by setting the speed of the variable speed motor with the speed controller at an upper speed, above the restricted speed zone and adjusting the inlet guide vanes to obtain the desired flow rate.
23. The method of claim 22, wherein, when the speed of the variable speed motor is set at the upper speed, above the restricted speed zone and the desired flow rate requires adjusting the speed of the variable speed motor to a speed below the restricted speed zone, the speed of the variable speed motor is decreased in decreasing speed steps until a lower speed, below the restricted speed zone, is obtained and the inlet guide vanes are successively opened during each of said decreasing speed steps such that the inlet guide vanes are set at the 0° swirl angle when the speed of the variable speed motor is at the lower speed, below the restricted speed zone.
24. The method of claim 21, wherein, when the speed of the variable speed motor is set below the restricted speed zone and the desired flow rate requires adjusting the speed of the variable speed motor to a new speed above the restricted speed zone, the speed of the variable speed motor is increased in increasing speed steps until the new speed, above the restricted speed zone, is obtained and the inlet guide vanes are successively closed during each of said increasing speed steps such that the position of the inlet guide vanes required to obtain the desired flow rate will be reached when the new speed, above the restricted speed zone is reached.
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