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US20170356451A1 - Copmpression unit for high and low pressure services - Google Patents

Copmpression unit for high and low pressure services Download PDF

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Publication number
US20170356451A1
US20170356451A1 US15/535,172 US201515535172A US2017356451A1 US 20170356451 A1 US20170356451 A1 US 20170356451A1 US 201515535172 A US201515535172 A US 201515535172A US 2017356451 A1 US2017356451 A1 US 2017356451A1
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United States
Prior art keywords
compression unit
unit
driver
overhung
shaft
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Abandoned
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US15/535,172
Inventor
Stefano Bresciani
Lorenza Sassolini
Nicola Banchi
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Nuovo Pignone Technologie SRL
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Nuovo Pignone SRL
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Filing date
Publication date
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Assigned to NUOVO PIGNONE SRL reassignment NUOVO PIGNONE SRL ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: BANCHI, NICOLA, BRESCIANI, STEFANO, SASSOLINI, LORENZA
Publication of US20170356451A1 publication Critical patent/US20170356451A1/en
Assigned to Nuovo Pignone Tecnologie S.r.l. reassignment Nuovo Pignone Tecnologie S.r.l. NUNC PRO TUNC ASSIGNMENT (SEE DOCUMENT FOR DETAILS). Assignors: NUOVO PIGNONE S.R.L.
Abandoned legal-status Critical Current

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04DNON-POSITIVE-DISPLACEMENT PUMPS
    • F04D17/00Radial-flow pumps, e.g. centrifugal pumps; Helico-centrifugal pumps
    • F04D17/08Centrifugal pumps
    • F04D17/10Centrifugal pumps for compressing or evacuating
    • F04D17/12Multi-stage pumps
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04DNON-POSITIVE-DISPLACEMENT PUMPS
    • F04D25/00Pumping installations or systems
    • F04D25/02Units comprising pumps and their driving means
    • 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
    • F04D25/16Combinations of two or more pumps ; Producing two or more separate gas flows
    • F04D25/163Combinations of two or more pumps ; Producing two or more separate gas flows driven by a common gearing arrangement
    • 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
    • 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
    • F25J3/04024Providing 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
    • 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
    • F25J3/04109Arrangements of compressors and /or their drivers
    • 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
    • F25J3/04109Arrangements of compressors and /or their drivers
    • F25J3/04145Mechanically coupling of different compressors of the air fractionation process to the same driver(s)
    • 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
    • F25J3/04151Purification and (pre-)cooling of the feed air; recuperative heat-exchange with product streams
    • F25J3/04163Hot end purification of the feed air
    • F25J3/04169Hot end purification of the feed air by adsorption of the impurities
    • F25J3/04175Hot end purification of the feed air by adsorption of the impurities at a pressure of substantially more than the highest pressure column
    • 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

Definitions

  • Embodiments of the present invention relate to a compression unit for supplying a complete pressure service to a plant, the single compression unit being capable of supplying high and low pressure services.
  • a main drawback of the prior art is the complexity of the overall architecture and configuration of the compression units, this leading to bulky apparatus.
  • each of such compression units comprising a dedicated driver and associated impellers which increase the overall dimensions of the units.
  • An embodiment of the present invention relates to a single compression unit for supplying a complete compression service consisting of high and low pressure gas to a process plant.
  • the compression unit is configured to supply high and low pressure gas flow with a simple architecture and with a configuration which reduces overall dimensions and weight of the unit, and also has an increased efficiency with respect to the state of the art.
  • impellers having a large diameter can process a high flow rate but work with reduced rotational speed and, therefore, a limited compression ratio.
  • the term “low” pressure here indicates rating values within a typical range comprised between 150 and 300, while the impeller can process a flow rate which could be comprised in a range between 50.000 and 200.000 m3 per hour.
  • a typical speed value of an impeller processing said flow rates is 5.000 to 1.800 rounds per minute thus indicated for a direct coupled solution.
  • high pressure here indicates typical rating values comprised between 300 and 2500, with an inlet pressure value between 3 and 50 bar for the first impeller.
  • the impeller processes low flow rates, typically less than 50.000 m3 per hour.
  • FIG. 1 is a schematic representation of one embodiment of the compression unit
  • FIG. 2 is a schematic representation of the compression unit according to an embodiment.
  • Such compression unit 1 comprises a single driver 2 associated with two driver shaft-ends, and in one embodiment projecting apart from said driver 2 along opposite directions, a first driver shaft end 3 and a second driver shaft end 4 .
  • the driver 2 divides the compression unit into two sides; on one side, a first unit 10 is operatively connected to the first driver shaft-end 3 , while a second unit 20 is operatively connected to the second driver shaft-end 4 .
  • said first unit 10 comprises an impeller 11
  • said second unit comprises a bull gear 21 in an integrally geared-compressor arrangement.
  • said impeller 11 of said first unit 10 is an overhung impeller directly connected to the first driver shaft-end 3 , and in one embodiment by means of a flanged connection or a flexible coupling.
  • an overhung impeller is an impeller having no bearing/s on the opposite side with respect to the driver, thus all bearing/s of the overhang impeller are arranged between the impeller and the driver.
  • the impeller 11 of the first unit is the “low” pressure source unit: typical values of flow rate processed by the overhung impeller are about 50.000 m3 per hour, with an inlet pressure value of around 1 bar and an outlet pressure value of about 2 or 3 bar.
  • the bull gear 21 is in one embodiment connected by means of a flanged connection, or a flexible coupling, to said second driver shaft-end 4 .
  • said second unit 20 comprises the bull gear 21 which drives at least one driven shaft 22 , 23 through pinions in a typical integrally geared-compressor arrangement.
  • the bull gear 21 comprises two or more driven shafts, for example a first driven shaft 22 and a second driven shaft 23 , which are drivingly connected to the bull gear 21 by means of respectively pinions.
  • Said pinions are teethed wheels having a diameter smaller than the diameter of the bull gear.
  • the pinions are engaged directly on the bull gear so that the rotation of the latter produces the rotation of pinions.
  • Each of said driven shafts supports at its opposite ends an overhung impeller 22 a , 22 b , 23 a , 23 b.
  • the two driven shafts 22 , 23 are configured to rotate at different rotary speed.
  • Typical flow rate values for the second unit 20 are about 50.000 and 200.000 m3 per hour, with casing rating varying between ANSI 300 and 1500.
  • the driver 2 drives the single overhung impeller 11 connected to said first driver shaft 3 .
  • the same driver 2 drives the bull gear 21 which comprises in one embodiment two driven shafts 22 , 23 , the first driven shaft 22 supports at its ends a couple of first overhung impellers 22 a , 22 b , the second driven shaft 23 supports at its ends a couple of second overhung impellers 23 a , 23 b.
  • the first overhung impellers 22 a , 22 b and the second overhung impellers 23 a , 23 b are fluidly connected so that the gas flow passes through the first overhung impellers 22 a , 22 b of the first driven shaft 22 and then through the second overhung impellers of the second driven shaft 23 , thus forming a first multi stage compression unit for compressing a small flow rate up to high pressure values.
  • This configuration is illustrated in FIG. 1 by means of dashed lines indicated with the reference number 40 which represent the hydraulic connection between the impellers.
  • the outlet of the overhung impeller 11 of the first unit 10 is fluidly connected to the inlet of the second unit 20 , thus forming a second multi stage compression unit.
  • This configuration is represented in FIG. 1 by means of dashed line 30 which represent the hydraulic connection between the units.
  • the first unit 10 provides the gas flow rate to the second unit 20 thus obtaining a compression unit apt to elaborate large flow rates with an high overall compression rate.
  • the first unit 10 comprises an overhung impeller 11 which is connected to said first driver shaft 3 by means of a gear arrangement, instead that flanged to said first driver shaft.
  • the first unit 10 comprises a beam compressor.
  • Said beam compressor may be flanged to said first driver shaft 3 or, alternatively, the beam compressor may be connected to said first driver shaft 3 by means of a gear arrangement.
  • Typical beam compressor casing rating varies from ANSI 600 to API 15000.
  • the inlet of the beam compressor may be hydraulically connected to the output of the bull gear 21 of the second unit 20 .
  • the first unit 10 receives the flow rate coming from the output of the second unit 20 , thus forming a third multi stage compression unit allowing to reach higher compression rates.
  • the hydraulic connection between the first 10 and the second 20 unit is represented in FIG. 2 by means of the dashed line 50 .
  • the compression unit according to an embodiment of the present invention therefore solves the drawbacks afflicting the prior art.
  • One of the results achieved with the compression unit according to the present invention is to reduce the footprint of the apparatus, with an extremely versatile configuration.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Structures Of Non-Positive Displacement Pumps (AREA)

Abstract

A compression unit for supplying high and low pressure services to a plant including a single driver associated with two driver shaft-ends projecting apart from the driver, a first driver shaft end and a second driver shaft end, a first unit being operatively connected to the first driver shaft-end and a second unit being operatively connected to the second driver shaft-end.

Description

    BACKGROUND
  • Embodiments of the present invention relate to a compression unit for supplying a complete pressure service to a plant, the single compression unit being capable of supplying high and low pressure services.
  • Within a process plant, to supply high pressure gas and low pressure gas several different units are usually provided to process different flow rates at different pressure values.
  • A main drawback of the prior art is the complexity of the overall architecture and configuration of the compression units, this leading to bulky apparatus.
  • In fact, usually separate units are used to provide gas at different pressure values to a process plant, each of such compression units comprising a dedicated driver and associated impellers which increase the overall dimensions of the units.
  • SUMMARY
  • An embodiment of the present invention relates to a single compression unit for supplying a complete compression service consisting of high and low pressure gas to a process plant.
  • The compression unit is configured to supply high and low pressure gas flow with a simple architecture and with a configuration which reduces overall dimensions and weight of the unit, and also has an increased efficiency with respect to the state of the art.
  • In order to better clarify what is to be intended with the terms “high” and “low” pressure reference to the compressor flanges rating, according to ANSI, will be done hereafter.
  • As known in the art, technical limits exist while designing an impeller. One of these limits is represented by the peripheral speed of the impeller.
  • It is known in the art that impellers having a large diameter can process a high flow rate but work with reduced rotational speed and, therefore, a limited compression ratio. In order to give typical values, the term “low” pressure here indicates rating values within a typical range comprised between 150 and 300, while the impeller can process a flow rate which could be comprised in a range between 50.000 and 200.000 m3 per hour.
  • A typical speed value of an impeller processing said flow rates is 5.000 to 1.800 rounds per minute thus indicated for a direct coupled solution.
  • The term “high” pressure here indicates typical rating values comprised between 300 and 2500, with an inlet pressure value between 3 and 50 bar for the first impeller. In order to reach very high compression rates, the impeller processes low flow rates, typically less than 50.000 m3 per hour.
  • BRIEF DESCRIPTION OF THE DRAWINGS
  • Further details and specific embodiments will refer to the attached drawing, in which:
  • FIG. 1 is a schematic representation of one embodiment of the compression unit;
  • FIG. 2 is a schematic representation of the compression unit according to an embodiment.
  • DETAILED DESCRIPTION
  • The following description of exemplary embodiments refers to the accompanying drawings. The following detailed description does not limit the invention. Instead, the scope of the invention is defined by the appended claims.
  • Reference throughout the specification to “one embodiment” or “an embodiment” means that a particular feature, structure, or characteristic described in connection with an embodiment is included in at least one embodiment of the subject matter disclosed. Thus, the appearance of the phrases “in one embodiment” or “in an embodiment” in various places throughout the specification is not necessarily referring to the same embodiment. Further, the particular features, structures or characteristics may be combined in any suitable manner in one or more embodiments.
  • Such compression unit 1 comprises a single driver 2 associated with two driver shaft-ends, and in one embodiment projecting apart from said driver 2 along opposite directions, a first driver shaft end 3 and a second driver shaft end 4.
  • In order to better describe the compression unit according to embodiments of the present invention, it can be considered that the driver 2 divides the compression unit into two sides; on one side, a first unit 10 is operatively connected to the first driver shaft-end 3, while a second unit 20 is operatively connected to the second driver shaft-end 4.
  • According to an embodiment of the present invention, said first unit 10 comprises an impeller 11, and said second unit comprises a bull gear 21 in an integrally geared-compressor arrangement.
  • More particularly, according to an embodiment said impeller 11 of said first unit 10 is an overhung impeller directly connected to the first driver shaft-end 3, and in one embodiment by means of a flanged connection or a flexible coupling.
  • According to an embodiment of the present invention, an overhung impeller is an impeller having no bearing/s on the opposite side with respect to the driver, thus all bearing/s of the overhang impeller are arranged between the impeller and the driver.
  • In this case, the impeller 11 of the first unit is the “low” pressure source unit: typical values of flow rate processed by the overhung impeller are about 50.000 m3 per hour, with an inlet pressure value of around 1 bar and an outlet pressure value of about 2 or 3 bar.
  • On the other side, the bull gear 21 is in one embodiment connected by means of a flanged connection, or a flexible coupling, to said second driver shaft-end 4.
  • According to an embodiment shown in FIG. 1, said second unit 20 comprises the bull gear 21 which drives at least one driven shaft 22, 23 through pinions in a typical integrally geared-compressor arrangement. In order to obtain higher outlet pressure values, the bull gear 21 comprises two or more driven shafts, for example a first driven shaft 22 and a second driven shaft 23, which are drivingly connected to the bull gear 21 by means of respectively pinions.
  • Said pinions are teethed wheels having a diameter smaller than the diameter of the bull gear. The pinions are engaged directly on the bull gear so that the rotation of the latter produces the rotation of pinions.
  • Each of said driven shafts supports at its opposite ends an overhung impeller 22 a, 22 b, 23 a, 23 b.
  • According to an embodiment of the present invention, the two driven shafts 22, 23 are configured to rotate at different rotary speed.
  • Typical flow rate values for the second unit 20 are about 50.000 and 200.000 m3 per hour, with casing rating varying between ANSI 300 and 1500.
  • According to the first embodiment of the compression unit 1 shown in FIG. 1, the driver 2 drives the single overhung impeller 11 connected to said first driver shaft 3.
  • On the other side of the compression unit 1, the same driver 2 drives the bull gear 21 which comprises in one embodiment two driven shafts 22, 23, the first driven shaft 22 supports at its ends a couple of first overhung impellers 22 a, 22 b, the second driven shaft 23 supports at its ends a couple of second overhung impellers 23 a, 23 b.
  • According to the scheme of FIG. 1, the first overhung impellers 22 a, 22 b and the second overhung impellers 23 a, 23 b are fluidly connected so that the gas flow passes through the first overhung impellers 22 a, 22 b of the first driven shaft 22 and then through the second overhung impellers of the second driven shaft 23, thus forming a first multi stage compression unit for compressing a small flow rate up to high pressure values. This configuration is illustrated in FIG. 1 by means of dashed lines indicated with the reference number 40 which represent the hydraulic connection between the impellers.
  • According to an embodiment of the present invention, the outlet of the overhung impeller 11 of the first unit 10 is fluidly connected to the inlet of the second unit 20, thus forming a second multi stage compression unit. This configuration is represented in FIG. 1 by means of dashed line 30 which represent the hydraulic connection between the units.
  • In this configuration, the first unit 10 provides the gas flow rate to the second unit 20 thus obtaining a compression unit apt to elaborate large flow rates with an high overall compression rate.
  • According to an embodiment of the present invention not shown in the drawings, the first unit 10 comprises an overhung impeller 11 which is connected to said first driver shaft 3 by means of a gear arrangement, instead that flanged to said first driver shaft.
  • According to an embodiment of the present invention shown in FIG. 2, the first unit 10 comprises a beam compressor. Said beam compressor may be flanged to said first driver shaft 3 or, alternatively, the beam compressor may be connected to said first driver shaft 3 by means of a gear arrangement.
  • Typical beam compressor casing rating varies from ANSI 600 to API 15000.
  • When the first unit 10 comprises a beam compressor, the inlet of the beam compressor may be hydraulically connected to the output of the bull gear 21 of the second unit 20. According to this arrangement, the first unit 10 receives the flow rate coming from the output of the second unit 20, thus forming a third multi stage compression unit allowing to reach higher compression rates. The hydraulic connection between the first 10 and the second 20 unit is represented in FIG. 2 by means of the dashed line 50.
  • The compression unit according to an embodiment of the present invention therefore solves the drawbacks afflicting the prior art.
  • One of the results achieved with the compression unit according to the present invention is to reduce the footprint of the apparatus, with an extremely versatile configuration.
  • This written description uses examples to disclose the invention, including the preferred embodiments, and also to enable any person skilled in the art to practice the invention, including making and using any devices or systems and performing any incorporated methods. The patentable scope of the invention is defined by the claims, and may include other examples that occur to those skilled in the art. Such other examples are intended to be within the scope of the claims if they have structural elements that do not differ from the literal language of the claims, or if they include equivalent structural elements with insubstantial differences from the literal languages of the claims.

Claims (11)

What is claimed is:
1. A compression unit for supplying high and low pressure services to a plant, the compression unit comprising:
a single driver associated with two driver shaft-ends projecting apart from the driver;
a first driver shaft end and a second driver shaft end; and
a first unit being directly operatively connected to the first driver shaft-end and a second unit being operatively connected to the second driver shaft-end,
wherein the first unit is an overhung impeller, and the second unit is an integrally geared-compressor arrangement comprising a bull gear and a plurality of pinions engaged with the bull gear, wherein the diameter of bull gear is larger than the diameter of pinions.
2. The compression unit according to claim 1, wherein the overhung impeller of the first unit is an impeller connected to the first driver shaft-end by a gear arrangement.
3. The compression unit according to claim 1, wherein the bull gear is connected by a flanged connection to the second driver shaft-end.
4. The compression unit according to claim 1, wherein the integrally geared-compressor arrangement comprises at least one driven shaft.
5. The compression unit according to claim 4, wherein at the opposite ends of the at least one driven shaft are provided overhung impellers.
6. The compression unit according to claim 4, wherein the bull gear comprises two driven shafts, a first driven shaft and a second driven shaft, each of the first and second driven shaft being provided at its ends with a couple of overhung impellers, respectively first overhung impellers and second overhung impellers.
7. The compression unit according to claim 1, wherein the first overhung impellers and the second overhung impellers are fluidly connected thus forming a first multi stage compression unit.
8. The compression unit according to claim 1, wherein an outlet of the first unit is fluidly connected to an inlet of the second unit, forming a second multi stage compression unit.
9. The compression unit according to claim 1, wherein the inlet of the first unit is fluidly connected to the outlet of the second unit, forming a third multi stage compression unit.
10. The compression unit according to claim 1, wherein the driver shaft-ends are the ends of a single driver shaft.
11. The compression unit according to claim 1, wherein the two driven shafts are configured to rotate at different rotary speeds.
US15/535,172 2014-12-16 2015-11-30 Copmpression unit for high and low pressure services Abandoned US20170356451A1 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
ITMI2014A002145 2014-12-16
ITMI20142145 2014-12-16
PCT/EP2015/078072 WO2016096386A1 (en) 2014-12-16 2015-11-30 Compression unit for high and low pressure services

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EP (1) EP3234370B1 (en)
JP (1) JP2018503766A (en)
CN (1) CN107429702A (en)
DK (1) DK3234370T3 (en)
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Cited By (2)

* Cited by examiner, † Cited by third party
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IT201800000620A1 (en) * 2018-01-08 2019-07-08 Nuovo Pignone Tecnologie Srl AMMONIA PRODUCTION PLANT
EP3617519A1 (en) * 2018-08-27 2020-03-04 Siemens Aktiengesellschaft Radially compressor rotor, radial compressor, gear-driven compressor

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN117905711B (en) * 2024-03-20 2024-07-23 江苏海拓宾未来工业科技集团有限公司 A multi-shaft centrifugal compressor and its impeller fault diagnosis method

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB202295A (en) * 1922-08-12 1924-06-05 Bbc Brown Boveri & Cie Improvements in multi-stage centrifugal compressors
US3809493A (en) * 1970-06-08 1974-05-07 Carrier Corp Interchangeable compressor drive
US5306117A (en) * 1991-12-23 1994-04-26 Nova Corporation Of America Axial inlet beam-type compressor
JP3457828B2 (en) * 1997-03-05 2003-10-20 三菱重工業株式会社 Compressor and gas expander device
EP2083172A1 (en) * 2008-01-22 2009-07-29 Siemens Aktiengesellschaft Multi-body compressor train
US20110008186A1 (en) * 2009-07-10 2011-01-13 Sergio Palomba High-pressure compression unit for process fluids for industrial plant and a related method of operation
CN102979751A (en) * 2012-09-25 2013-03-20 西安交大赛尔机泵成套设备有限责任公司 Single-shaft plusing multiple-shaft type carbon dioxide gas centrifugal compressor unit

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4416497C1 (en) * 1994-05-10 1995-01-12 Gutehoffnungshuette Man Geared multi-shaft turbo-compressor and geared multi-shaft radial expander
CN101435428B (en) * 2008-12-22 2010-11-03 重庆朝阳气体有限公司 High and low pressure operation double-mode double-cylinder centrifugal type oxygen pressure machine
US20110097225A1 (en) * 2009-10-28 2011-04-28 Freund Sebastian W Air compression and expansion system with single shaft compressor and turbine arrangement
US20150211539A1 (en) * 2014-01-24 2015-07-30 Air Products And Chemicals, Inc. Systems and methods for compressing air

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB202295A (en) * 1922-08-12 1924-06-05 Bbc Brown Boveri & Cie Improvements in multi-stage centrifugal compressors
US3809493A (en) * 1970-06-08 1974-05-07 Carrier Corp Interchangeable compressor drive
US5306117A (en) * 1991-12-23 1994-04-26 Nova Corporation Of America Axial inlet beam-type compressor
JP3457828B2 (en) * 1997-03-05 2003-10-20 三菱重工業株式会社 Compressor and gas expander device
EP2083172A1 (en) * 2008-01-22 2009-07-29 Siemens Aktiengesellschaft Multi-body compressor train
US20110008186A1 (en) * 2009-07-10 2011-01-13 Sergio Palomba High-pressure compression unit for process fluids for industrial plant and a related method of operation
CN102979751A (en) * 2012-09-25 2013-03-20 西安交大赛尔机泵成套设备有限责任公司 Single-shaft plusing multiple-shaft type carbon dioxide gas centrifugal compressor unit

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
IT201800000620A1 (en) * 2018-01-08 2019-07-08 Nuovo Pignone Tecnologie Srl AMMONIA PRODUCTION PLANT
EP3508447A1 (en) * 2018-01-08 2019-07-10 Nuovo Pignone Tecnologie SrL Ammonia production plant
KR20190084872A (en) * 2018-01-08 2019-07-17 누보 피그노네 테크놀로지 에스알엘 Ammonia production plant
CN110028082A (en) * 2018-01-08 2019-07-19 诺沃皮尼奥内技术股份有限公司 Ammonia production equipment
JP2019151545A (en) * 2018-01-08 2019-09-12 ヌオーヴォ・ピニォーネ・テクノロジー・ソチエタ・レスポンサビリタ・リミタータNuovo Pignone Tecnologie S.R.L. Ammonia production plant
US10457564B2 (en) 2018-01-08 2019-10-29 Nuovo Pignone Tecnologie Srl Ammonia production plant
JP7300836B2 (en) 2018-01-08 2023-06-30 ヌオーヴォ・ピニォーネ・テクノロジー・ソチエタ・レスポンサビリタ・リミタータ Ammonia production plant
KR102664151B1 (en) 2018-01-08 2024-05-07 누보 피그노네 테크놀로지 에스알엘 Ammonia production plant
EP3617519A1 (en) * 2018-08-27 2020-03-04 Siemens Aktiengesellschaft Radially compressor rotor, radial compressor, gear-driven compressor
WO2020043379A1 (en) * 2018-08-27 2020-03-05 Siemens Aktiengesellschaft Radial compressor rotor, radial compressor, geared compressor

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