AU2013395108B2 - Refrigeration compression system using two compressors - Google Patents

Refrigeration compression system using two compressors Download PDF

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AU2013395108B2
AU2013395108B2 AU2013395108A AU2013395108A AU2013395108B2 AU 2013395108 B2 AU2013395108 B2 AU 2013395108B2 AU 2013395108 A AU2013395108 A AU 2013395108A AU 2013395108 A AU2013395108 A AU 2013395108A AU 2013395108 B2 AU2013395108 B2 AU 2013395108B2
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compressor
outlet
refrigeration circuit
inlet
casing
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Yoshitsugi Kikkawa
Hirohiko Kikuchi
Toshiya MOMOSE
Masaaki Oishi
Koichiro SAKAI
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Chiyoda Corp
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Chiyoda Corp
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    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/0002—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the fluid to be liquefied
    • F25J1/0022—Hydrocarbons, e.g. natural gas
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/003—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production
    • F25J1/0047—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production using an "external" refrigerant stream in a closed vapor compression cycle
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B40/00—Subcoolers, desuperheaters or superheaters
    • F25B40/04—Desuperheaters
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/003—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production
    • F25J1/0047—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production using an "external" refrigerant stream in a closed vapor compression cycle
    • F25J1/0052—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production using an "external" refrigerant stream in a closed vapor compression cycle by vaporising a liquid refrigerant stream
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/003—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production
    • F25J1/0047—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production using an "external" refrigerant stream in a closed vapor compression cycle
    • F25J1/0052—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production using an "external" refrigerant stream in a closed vapor compression cycle by vaporising a liquid refrigerant stream
    • F25J1/0055—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production using an "external" refrigerant stream in a closed vapor compression cycle by vaporising a liquid refrigerant stream originating from an incorporated cascade
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/006—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the refrigerant fluid used
    • F25J1/008—Hydrocarbons
    • F25J1/0087—Propane; Propylene
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/02—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process
    • F25J1/0211—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process using a multi-component refrigerant [MCR] fluid in a closed vapor compression cycle
    • F25J1/0214—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process using a multi-component refrigerant [MCR] fluid in a closed vapor compression cycle as a dual level refrigeration cascade with at least one MCR cycle
    • F25J1/0215—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process using a multi-component refrigerant [MCR] fluid in a closed vapor compression cycle as a dual level refrigeration cascade with at least one MCR cycle with one SCR cycle
    • F25J1/0216—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process using a multi-component refrigerant [MCR] fluid in a closed vapor compression cycle as a dual level refrigeration cascade with at least one MCR cycle with one SCR cycle using a C3 pre-cooling cycle
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/02—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process
    • F25J1/0243—Start-up or control of the process; Details of the apparatus used; Details of the refrigerant compression system used
    • F25J1/0279—Compression of refrigerant or internal recycle fluid, e.g. kind of compressor, accumulator, suction drum etc.
    • F25J1/0281—Compression of refrigerant or internal recycle fluid, e.g. kind of compressor, accumulator, suction drum etc. characterised by the type of prime driver, e.g. hot gas expander
    • F25J1/0283—Gas turbine as the prime mechanical driver
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/02—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process
    • F25J1/0243—Start-up or control of the process; Details of the apparatus used; Details of the refrigerant compression system used
    • F25J1/0279—Compression of refrigerant or internal recycle fluid, e.g. kind of compressor, accumulator, suction drum etc.
    • F25J1/0294—Multiple compressor casings/strings in parallel, e.g. split arrangement
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B1/00—Compression machines, plants or systems with non-reversible cycle
    • F25B1/10—Compression machines, plants or systems with non-reversible cycle with multi-stage compression
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2400/00—General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
    • F25B2400/13—Economisers
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2400/00—General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
    • F25B2400/23—Separators

Abstract

Apparatus for compressing gaseous refrigerant for use in a refrigeration circuit of a liquefaction plant comprises a refrigeration circuit (1) and two compressors (10, 20) that are functionally connected to the refrigeration circuit. One of the compressors is provided with a double suction configuration, and the outlets and the inlets of the first and second compressors are connected at least partly in a mutually parallel flow configuration such that the refrigerant flow that leaves the refrigeration circuit from a plurality of outlets thereof is distributed between the two compressors before joining at the inlet of the refrigeration circuit.

Description

Description
Title of Invention: REFRIGERATION COMPRESSION SYSTEM USING TWO COMPRESSORS
Technical Field [0001] The present invention relates to a refrigeration compression system for use in a refrigeration circuit of a liquefaction plant, and in particular to a refrigeration compression system that can be constructed as a compact unit for a given production rate.
Background Art [0002] Natural gas is known to be environmentally favorable as compared with other fossil fuels and nuclear fuels, but is required to be processed in an appropriate manner before it can be delivered to the final users. The cost for such processing is highly important for the natural gas to be competitive with other forms of fuels. Most significantly, natural gas is most often required to be liquefied for the convenience of storage and delivery to the final users, and the cost of liquefaction accounts for a large part of the cost of natural gas. In large liquefaction plants, liquefaction of natural gas is usually accomplished by compressing the natural gas by using a series of compressors which are powered by gas turbine drivers, and removing heat from the compressed natural gas by using heat exchangers.
[0003] In general, the cost of liquefaction can be reduced by using a refrigerant system with a higher refrigeration duty. The C3 MR (propane pre-cooled mixed refrigerant process) and the optimized cascade process are the two processes that are currently most widely used. These processes use C3 refrigerant for the pre-cooling of the process flow, and it is the pre-cooling process that imposes the most critical design issue in increasing the production rate of the system.
[0004] The production rate of the pre-cooling process can be increased by using larger compressors that can accommodate larger inlet volumes, but there is a limit to the size of the compressors for the given driver speed. A simple method to increase the compressor inlet volume is to increase the impeller diameter. However, the required yield strength of the impeller tip would increase so sharply as the impeller diameter is increased that the difficulty and cost of manufacture become unacceptable once a certain limit is reached. Also, as the inlet flow Mach number is increased, the operating range of the compressor is narrowed, and the efficiency of the compressor starts dropping sharply. The problem is particularly acute because the sonic velocity in LP C3 refrigerant is very low, typically approximately 230 m/sec. As a result, the impeller size at the LP stage would be limited below 1,320 mm when the rotor speed is selected at the typically speed of 3,600 rpm.
2013395108 19 Jan 2018
-2[0005] Also, the last stage of the compressor must treat a high volume flow particularly when a side-stream compressor machine is used as is often the case in large refrigeration plants. This will lead to a drop in aerodynamic performance because of the need to select a large flow coefficient impeller in order to handle the large flow rate with a limited size of the impeller.
[0006] The flow coefficient is one of the dimensionless quantities used by the manufacturers to show the impeller performance, and is expressed by the formula given below.
F = Qo/ {(pi/4)D2U2} where F: flow coefficient β
Q: suction volume flow (m /sec)
D: impeller diameter (m)
U2: impeller tip speed (m/s)
The proven range of the flow coefficient is below 0.155.
[0007] A liquefaction plant typically employs a number of identical compressor trains. Therefore, designing the compressor trains in an optimum fashion is highly important in increasing the efficiency of the liquefaction plant.
[0008] The production rate of a C3 can be increased by using two compressors of a limited size in separate casings in a 50%-50% parallel scheme. However, this scheme requires a large amount of piping in an exactly symmetric 3D configuration, and the necessary material and labor cost prevents it from becoming a practical solution.
[0009] It was proposed in US6,637,238 and US6,962,060 to use two compressors with the aim of minimizing the mass flow rate at the higher pressure ends. The outlets of the two compressors are commonly connected, and the main and side inlets of the two compressors are connected to various outlets of the refrigeration circuit. However, the previous proposals are not entirely satisfactory in limiting the flow velocity at the lower pressure inlet of the corresponding compressor.
SUMMARY OF THE INVENTION [0010] In view of such problems of the prior art, the present invention desirably provides apparatus for compressing gaseous refrigerant for use in a refrigeration circuit of a liquefaction plant which is highly compact and can still maximize the product output rate.
[0011] It is also desirable that the present invention provides apparatus for compressing gaseous refrigerant which can maximize the product output rate by using readily available, relatively inexpensive compressors.
[0012] It is also desirable that the present invention provides apparatus for compressing gaseous refrigerant which can maximize the product output rate without suffering from the problem of reduced efficiency.
2013395108 03 Jul 2018
-3[0013] According to the present invention, there is provided for compressing gaseous refrigerant for use in a refrigeration circuit of a liquefaction plant, the apparatus comprising: a refrigeration circuit including an inlet for refrigerant at a refrigeration pressure, a low pressure outlet for gaseous refrigerant at a low pressure, a high pressure outlet for gaseous refrigerant at a high pressure and at least one intermediate pressure outlet for gaseous refrigerant at an intermediate pressure; a first compressor received in a first casing and provided with a double suction configuration including at least two main inlets defined on either axial ends of the casing and one outlet defined in an axially middle part of the casing; a second compressor received in a second casing separate from the first casing and having an at least one main inlet, a first side inlet, a second side inlet for a higher pressure input than the first side inlet, and an outlet; and a common power source including an output shaft for driving the first and second compressors; wherein the outlet of the first compressor is connected to the second side inlet of the second compressor, and the outlet of the second compressor is connected to the inlet of the refrigeration circuit; and wherein the low pressure outlet of the refrigeration circuit is connected to the main inlets of the first compressor, the at least one intermediate pressure outlet of the refrigeration circuit is connected to the main inlet of the second compressor, and the high pressure outlet of the refrigeration circuit is connected to the first side inlet of the second compressor.
[0014] The use of a double suction compressor for the first compressor allows the flow rate at the main inlets of the first compressor to be maximized without excessively increasing the flow velocity at the inlets. Typically, the two main inlets of the first compressor are commonly connected in a symmetric configuration. The outlets and the inlets of the first and second compressors being connected at least partly in a mutually parallel flow configuration means that the refrigerant flow that leaves the refrigeration circuit from a plurality of outlets thereof is distributed between the two compressors before joining at the inlet of the refrigeration circuit. The second compressor may be further provided with a third side inlet, the third inlet being connected to another of the intermediate pressure outlets of the refrigeration circuit.
[0015] As the two main inlets of the first compressor are connected to the low pressure outlet of the refrigeration circuit, the flow rate of the low pressure gaseous refrigerant may be maximized without excessively increasing the flow velocity of the low pressure gaseous refrigerant.
[0016] According to a certain aspect of the present invention, the first compressor is further provided with a pair of side inlets in a symmetric configuration that are connected to the intermediate pressure outlet of the refrigeration circuit. In certain embodiments, the first compressor has no side inlets.
2013395108 03 Jul 2018
-4[0017] The second compressor may be provided with either a straight suction configuration or a double suction configuration. If the second compressor is provided with a straight suction configuration, the outlet of the second compressor may be connected to the inlet of the refrigeration circuit via an economizer so that an economical operation of the refrigeration compression system can be achieved even when the available power of the compressor driver is not sufficient. The two main inlets of the first compressor may also be connected to different outlets of the refrigeration circuit. In such a case, the first compressor having a double suction configuration may be provided with either a symmetric or asymmetric configuration.
[0018] The refrigeration circuit typically comprises two intermediate pressure outlets for gaseous refrigerant at intermediate pressures, but may also be provided with one, three or more intermediate pressure outlets.
[0019] If the outlet of the first compressor as well as the outlet of the second compressor is connected to the inlet of the refrigeration circuit, the mass flow rate of the highest pressure gaseous refrigerant can be divided between the two compressors, and the mass flow rate at the outlet of each compressor can be avoided from become excessive.
BRIEF DESCRIPTION OF DRAWINGS [0020] Now the present invention is described in the following with reference to the appended drawings, in which:
Fig. la is a schematic diagram of a first embodiment of the apparatus for compressing gaseous refrigerant according to the present invention;
Fig. lb is a view similar to Fig. la showing a modification of the first embodiment; Fig. 2a is a view similar to Fig. la showing a second embodiment of the present invention;
Fig. 2b is a view similar to Fig. 2a showing a modification of the second embodiment; and
Figs. 3 to 20 are views similar to Fig. la showing other embodiments of the present
Figure AU2013395108B2_D0001
2013395108 19 Jan 2018
-5 DESCRIPTION OF THE PREFERRED EMBODIMENTS [0021] Fig. la shows a first embodiment of the apparatus for compressing gaseous refrigerant according to the present invention. This embodiment, as well as the other embodiments discussed in the following, is particularly suited for use in the C3MR process. For the details of the C3 MR (propane pre-cooled mixed refrigerant process), reference may be made to US5,832,745. However, the present invention may also be used in other applications where refrigerant is cooled by using a refrigeration circuit having a plurality of outlets and a compressor system including a plurality of stages corresponding to the outlets of the refrigeration circuit.
[0022] This apparatus comprises a propane (C3) refrigeration circuit 1 which includes an inlet 2 and four outlets 3, 4, 5 and 6 for refrigerant at different temperatures and pressures. In the illustrated embodiment, the four outlets consist of a low pressure (LP) outlet 6 for refrigerant at -40deg. C and 112.5kPa, a medium pressure (MP) outlet 5 for refrigerant at -21 deg. C and 234.5kPa, a high pressure (HP) outlet 4 for refrigerant at -6.6 deg. C and 384.8kPa, and a high high pressure (HHP) outlet 3 for refrigerant at 16.3 deg. C and 757.7kPa.
[0023] This apparatus comprises a first compressor 10 having a double suction configuration and a second compressor 20 having a straight suction configuration. The first compressor 10 is received in a single casing receiving two sets of impellers in a symmetric arrangement such that a pair of main inlets 12 and 13 are defined on either axial end of the casing, and an outlet 11 is defined in an axially middle part of the casing. Each set of impellers may include any number of impeller disks which are typically supported by a common shaft.
[0024] The second compressor 20 is also received in a single casing, and includes a plurality of impeller disks arranged in series along the axial length thereof and typically supported by a common shaft. The casing of the second compressor 20 defines an outlet 21 at an axial end thereof, a first inlet 22 at the other axial end thereof, and three more additional four inlets 23, 24 and 25 in axially intermediate positions thereof. The two compressors 10 and 20 are driven by an output shaft 31 of a common gas turbine driver 30. It is also possible to use other drive sources such as an electric motor or electric motors, instead of the gas turbine driver.
[0025] The LP outlet of the refrigeration circuit 1 is connected to the two main inlets 12 and 13 of the first compressor 10, and the outlet 11 of the first compressor 10 is connected to the high high high (HHHP) inlet 25 of the second compressor 20. The MP outlet 5 of the refrigeration circuit 1 is connected to the main inlet 22 of the second compressor 20, and the HP outlet 4 and the HHP outlet 3 of the refrigeration circuit 1 are connected to the HP and HHP inlets 23 and 24 of the second compressor
2013395108 19 Jan 2018
- 5a 20, respectively. The outlet 21 of the second compressor 20 is connected to the inlet 2 of the refrigeration circuit 1.
[0026] Alternatively, the HHHP inlet 25 may be omitted, and the outlet 11 of the first compressor 10 may be directly connected to the inlet 2 of the refrigeration circuit 1 as indicated by the dotted line in Fig. la. It should be noted that connecting the outlet of the first compressor 10 to an HHHP inlet of the second compressor 20, instead of the inlet 2 of the refrigeration circuit 1 is an option also in other embodiments, wherever applicable, which will be described hereinafter.
[0027] Fig. lb shows a modification of the first embodiment which is similar to the first embodiment except for the provision of an economizer circuit in the outlet circuit that can be used for reducing the flow rate of the refrigerant and hence the power consumption of the gas turbine driver 30.
[0028] The outlet 21 of the second compressor 20 is connected to an inlet of a desuperheater 41, instead of being connected directly to the inlet 2 of the refrigeration circuit 1. The outlet of the desuperheater 41 is connected to an economizer 44 via a condenser 42, an accumulator 43 and an adjustment valve 45, in that order. The economizer 44 is also connected to a high high high (HHHP) inlet 25 of the second compressor 20 (or the outlet 11 of the first compressor 10), and to the inlet 2 of the refrigeration circuit
Figure AU2013395108B2_D0002
WO 2015/011742 PCT/JP2013/004568 [0029] In this embodiment, by suitably adjusting the adjustment valve 45, the refrigerant flow can be adjusted depending on the demand for the refrigerant. This economizer circuit can also be optionally included in any of the following embodiments which will be described hereinafter, where the second compressor 20 is provided with a straight suction configuration.
[0030] Fig. 2a shows a second embodiment of the apparatus for compressing gaseous refrigerant according to the present invention. The apparatus of the second embodiment comprises a first compressor 10 having a double suction configuration and a second compressor 20 having a straight suction configuration. The first compressor 10 includes a pair of main inlets 12 and 13 defined on either axial end of the casing, a pair of side inlets 14 and 15 and an outlet 11 defined in an axially middle part of the casing, preferably all in a symmetric arrangement. Each set of impellers may include any number of impeller disks which are typically supported by a common shaft.
[0031] The second compressor 20 includes a plurality of impeller disks arranged in series along the axial length thereof. The casing of the second compressor 20 defines an outlet 21 at an axial end thereof, a main inlet 22 at the other axial end thereof and a single side inlet 23 in an axially intermediate position thereof. The two compressors 10 and 20 are driven by an output shaft 31 of a common gas turbine driver 30.
[0032] The FP outlet 6 of the refrigeration circuit 1 is connected to the main inlet 22 of the second compressor 20, and the MP outlet 5 of the refrigeration circuit 1 is connected to the two main inlets 12 and 13 of the first compressor 10. The HP outlet 4 of the refrigeration circuit 1 is connected to the two side inlets 14 and 15 of the first compressor 10, and the HHP outlet 3 of the refrigeration circuit 1 is connected to the side inlet 23 of the second compressor 20. The outlet 11 of the first compressor 10 and the outlet 21 of the second compressor 20 are both connected to the inlet 2 of the refrigeration circuit 1.
[0033] Fig. 2b shows a modification of the second embodiment which is similar to the second embodiment except for the provision of an economizer circuit in the outlet circuit that can be used for reducing the flow rate of the refrigerant and hence the power consumption of the gas turbine driver 30.
[0034] The outlet 21 of the second compressor 20 is connected to an inlet of a desuperheater 41, instead of being connected directly to the inlet 2 of the refrigeration circuit 1. The outlet of the desuperheater 41 is connected to an economizer 44 via a condenser 42, an accumulator 43 and an adjustment valve 45, in that order. The economizer 44 is also connected to a high high high (HHHP) inlet 25 of the second compressor 20 and to the inlet 2 of the refrigeration circuit 1. The outlet 11 of the first compressor 10 is connected to the high high high (HHHP) inlet 25 of the second compressor 20.
[0035] In this embodiment, by suitably adjusting the adjustment valve 45, the refrigerant
Ί
WO 2015/011742
PCT/JP2013/004568 flow can be adjusted depending on the demand for the refrigerant. This economizer circuit can also be optionally included in any of the following embodiments which will be described hereinafter, where the second compressor 20 is provided with a straight suction configuration.
[0036] Fig. 3 shows a third embodiment of the apparatus for compressing gaseous refrigerant according to the present invention. In Fig. 3, the parts corresponding to those of the previous embodiment without necessarily repeating the description of such parts.
[0037] The apparatus of the third embodiment comprises a first compressor 10 having a double suction configuration and a second compressor 20 having a straight suction configuration. The first compressor 10 includes a pair of main inlets 12 and 13 defined on either axial end of the casing, a pair of side inlets 14 and 15 and an outlet 11 defined in an axially middle part of the casing, preferably all in a symmetric arrangement. Each set of impellers may include any number of impeller disks which are typically supported by a common shaft.
[0038] The second compressor 20 includes a plurality of impeller disks arranged in series along the axial length thereof and typically supported by a common shaft. The casing of the second compressor 20 defines an outlet 21 at an axial end thereof, a main inlet 22 at the other axial end thereof, and a single side inlet 23 in an axially intermediate position thereof. The two compressors 10 and 20 are driven by an output shaft 31 of a common gas turbine driver 30.
[0039] The FP outlet 6 of the refrigeration circuit 1 is connected to the two main inlets 12 and 13 of the first compressor 10, and the MP outlet 5 of the refrigeration circuit 1 is connected to the two side inlets 14 and 15 of the first compressor 10. The HP outlet 4 of the refrigeration circuit 1 is connected to the main inlet 22 of the second compressor 20, and the HHP outlet 3 of the refrigeration circuit 1 is connected to the side inlet 23 of the second compressor 20. The outlet 21 of the first compressor 10 and the outlet 21 of the second compressor 20 are both connected to the inlet 2 of the refrigeration circuit 1.
[0040] Fig. 4 shows a fourth embodiment of the apparatus for compressing gaseous refrigerant according to the present invention. In Fig. 4 and other drawings showing different embodiments of the present invention which are to be described hereinafter, the parts corresponding to those of the preceding embodiments are denoted with like numerals without necessarily repeating the description of such parts.
[0041] The apparatus of the fourth embodiment comprises a first compressor 10 having a double suction configuration and a second compressor 20 also having a double suction configuration. The first compressor 10 includes a pair of main inlets 12 and 13 defined on either axial end of the casing, a pair of side inlets 14 and 15 and an outlet 11 defined in an axially middle part of the casing, preferably all in a symmetric arrangement. Each
WO 2015/011742
PCT/JP2013/004568 set of impellers may include any number of impeller disks which are typically supported by a common shaft.
[0042] The second compressor 20 also includes a pair of main inlets 22 and 23 defined on either axial end of the casing, a pair of side inlets 24 and 25 and an outlet 21 defined in an axially middle part of the casing, preferably all in a symmetric arrangement. Each set of impellers may include any number of impeller disks which are typically supported by a common shaft. The two compressors 10 and 20 are driven by an output shaft 31 of a common gas turbine driver 30.
[0043] The LP outlet 6 of the refrigeration circuit 1 is connected to the two main inlets 12 and 13 of the first compressor 10, and the MP outlet 5 of the refrigeration circuit 1 is connected to the two side inlets 14 and 15 of the first compressor 10. The HP outlet 4 of the refrigeration circuit 1 is connected to the main inlets 22 and 23 of the second compressor 20, and the HHP outlet 3 of the refrigeration circuit 1 is connected to the side inlets 24 and 25 of the second compressor 20. The outlet 11 of the first compressor 10 and the outlet 21 of the second compressor 20 are both connected to the inlet 2 of the refrigeration circuit 1.
[0044] Fig. 5 shows a fifth embodiment of the apparatus for compressing gaseous refrigerant according to the present invention. The apparatus of the fifth embodiment comprises a first compressor 10 having a double suction configuration and a second compressor 20 also having a double suction configuration. The first compressor 10 includes a pair of main inlets 12 and 13 defined on either axial end of the casing, a pair of side inlets 14 and 15 and an outlet 11 defined in an axially middle part of the casing, preferably all in a symmetric arrangement. Each set of impellers may include any number of impeller disks which are typically supported by a common shaft.
[0045] The second compressor 20 also includes a pair of main inlets 22 and 23 defined on either axial end of the casing, a pair of side inlets 24 and 25 and an outlet 21 defined in an axially middle part of the casing, preferably all in a symmetric arrangement. Each set of impellers may include any number of impeller disks which are typically supported by a common shaft. The two compressors 10 and 20 are driven by an output shaft 31 of a common gas turbine driver 30.
[0046] The LP outlet 6 of the refrigeration circuit 1 is connected to the two main inlets 12 and 13 of the first compressor 10, and the MP outlet 5 of the refrigeration circuit 1 is connected to the main inlets 22 and 23 of the second compressor 20. The HP outlet 4 of the refrigeration circuit 1 is connected to the side inlets 24 and 25 of the second compressor 20, and the HHP outlet 3 of the refrigeration circuit 1 is connected to the two side inlets 14 and 15 of the first compressor 10. The outlet 11 of the first compressor 10 and the outlet 21 of the second compressor 20 are both connected to the inlet 2 of the refrigeration circuit 1.
WO 2015/011742 PCT/JP2013/004568 [0047] Fig. 6 shows a sixth embodiment of the apparatus for compressing gaseous refrigerant according to the present invention. The apparatus of the sixth embodiment comprises a first compressor 10 having a double suction configuration and a second compressor 20 also having a double suction configuration. The first compressor 10 includes a pair of main inlets 12 and 13 defined on either axial end of the casing, a pair of side inlets 14 and 15 and an outlet 11 defined in an axially middle part of the casing, preferably all in a symmetric arrangement. Each set of impellers may include any number of impeller disks which are typically supported by a common shaft.
[0048] The second compressor 20 also includes a pair of main inlets 22 and 23 defined on either axial end of the casing, a pair of side inlets 24 and 25 and an outlet 21 defined in an axially middle part of the casing, preferably all in a symmetric arrangement. Each set of impellers may include any number of impeller disks which are typically supported by a common shaft. The two compressors 10 and 20 are driven by an output shaft 31 of a common gas turbine driver 30.
[0049] The EP outlet 6 of the refrigeration circuit 1 is connected to the two main inlets 12 and 13 of the first compressor 10, and the MP outlet 5 of the refrigeration circuit 1 is connected to the main inlets 22 and 23 of the second compressor 20. The HP outlet 4 of the refrigeration circuit 1 is connected to the two side inlets 14 and 15 of the first compressor 10, and the HHP outlet 3 of the refrigeration circuit 1 is connected to the side inlets 24 and 25 of the second compressor 20. The outlet 11 of the first compressor 10 and the outlet 21 of the second compressor 20 are both connected to the inlet 2 of the refrigeration circuit 1.
[0050] Fig. 7 shows a seventh embodiment of the apparatus for compressing gaseous refrigerant according to the present invention. The apparatus of the seventh embodiment comprises a first compressor 10 having a double suction configuration and a second compressor 20 having a straight suction configuration. The first compressor 10 includes a pair of main inlets 12 and 13 defined on either axial end of the casing, a pair of side inlets 14 and 15, and an outlet 11 defined in an axially middle part of the casing, preferably all in a symmetric arrangement. Each set of impellers may include any number of impeller disks which are typically supported by a common shaft.
[0051] The second compressor 20 includes a plurality of impeller disks arranged in series along the axial length thereof. The casing of the second compressor 20 defines an outlet 21 at an axial end thereof, a main inlet 22 at the other axial end thereof and a single side inlet 23 in an axially intermediate position thereof. The two compressors 10 and 20 are driven by an output shaft 31 of a common gas turbine driver 30.
[0052] The LP outlet 6 of the refrigeration circuit 1 is connected to the two main inlets 12 and 13 of the first compressor 10, and the MP outlet 5 of the refrigeration circuit 1 is connected to the main inlet 22 of the second compressor 20, and the HP outlet 4 of the
WO 2015/011742
PCT/JP2013/004568 refrigeration circuit 1 is connected to the two side inlets 14 and 15 of the first compressor 10, and the HHP outlet 3 of the refrigeration circuit 1 is connected to the side inlet 23 of the second compressor 20. The outlet 11 of the first compressor 10 and the outlet 21 of the second compressor 20 are both connected to the inlet 2 of the refrigeration circuit 1.
[0053] Fig. 8 shows an eighth embodiment of the apparatus for compressing gaseous refrigerant according to the present invention. The apparatus of the eighth embodiment comprises a first compressor 10 having a double suction configuration and a second compressor 20 having a straight suction configuration. The first compressor 10 includes a pair of main inlets 12 and 13 defined on either axial end of the casing, a pair of side inlets 14 and 15 and an outlet 11 defined in an axially middle part of the casing, preferably all in a symmetric arrangement. Each set of impellers may include any number of impeller disks which are typically supported by a common shaft.
[0054] The second compressor 20 includes a plurality of impeller disks arranged in series along the axial length thereof. The casing of the second compressor 20 defines an outlet 21 at an axial end thereof, a main inlet 22 at the other axial end thereof and a single side inlet 23 in an axially intermediate position thereof. The two compressors 10 and 20 are driven by an output shaft 31 of a common gas turbine driver 30.
[0055] The FP outlet 6 of the refrigeration circuit 1 is connected to the two main inlets 12 and 13 of the first compressor 10, and the MP outlet 5 of the refrigeration circuit 1 is connected to the main inlet 22 of the second compressor 20. The HP outlet 4 of the refrigeration circuit 1 is connected to the side inlet 23 of the second compressor 20, and the HHP outlet 3 of the refrigeration circuit 1 is connected to the two side inlets 14 and 15 of the first compressor 10. The outlet 11 of the first compressor 10 and the outlet 21 of the second compressor 20 are both connected to the inlet 2 of the refrigeration circuit 1.
[0056] Fig. 9 shows a ninth embodiment of the apparatus for compressing gaseous refrigerant according to the present invention. The apparatus of the ninth embodiment comprises a first compressor 10 having a double suction configuration and a second compressor 20 having a straight suction configuration. The first compressor 10 includes a pair of main inlets 12 and 13 defined on either axial end of the casing and an outlet 11 defined in an axially middle part of the casing, preferably all in a symmetric arrangement. Each set of impellers may include any number of impeller disks which are typically supported by a common shaft.
[0057] The second compressor 20 includes a plurality of impeller disks arranged in series along the axial length thereof. The casing of the second compressor 20 defines an outlet 21 at an axial end thereof, a main inlet 22 at the other axial end thereof, and a pair of side inlets 23 and 24 in axially intermediate positions thereof. The two com11
WO 2015/011742
PCT/JP2013/004568 pressors 10 and 20 are driven by an output shaft 31 of a common gas turbine driver 30.
[0058] The LP outlet 6 of the refrigeration circuit 1 is connected to the main inlet 22 of the second compressor 20, and the MP outlet 5 of the refrigeration circuit 1 is connected to the two main inlets 12 and 13 of the first compressor 10. The HP outlet 4 of the refrigeration circuit 1 is connected to the one of the side inlets 23 (lower pressure side) of the second compressor 20, and the HHP outlet 3 of the refrigeration circuit 1 is connected to the other side inlet 24 (higher pressure side) of the second compressor 20. The outlet 11 of the first compressor 10 and the outlet 21 of the second compressor 20 are both connected to the inlet 2 of the refrigeration circuit 1.
[0059] Fig. 10 shows a tenth embodiment of the apparatus for compressing gaseous refrigerant according to the present invention. The apparatus of the tenth embodiment comprises a first compressor 10 having a double suction configuration and a second compressor 20 having a straight suction configuration. The first compressor 10 includes a pair of main inlets 12 and 13 defined on either axial end of the casing and an outlet 11 defined in an axially middle part of the casing, preferably all in a symmetric arrangement. Each set of impellers may include any number of impeller disks which are typically supported by a common shaft.
[0060] The second compressor 20 includes a plurality of impeller disks arranged in series along the axial length thereof. The casing of the second compressor 20 defines an outlet 21 at an axial end thereof, a main inlet 22 at the other axial end thereof and a pair of side inlets 23 and 24 in axially intermediate positions thereof. The two compressors 10 and 20 are driven by an output shaft 31 of a common gas turbine driver 30.
[0061] The FP outlet 6 of the refrigeration circuit 1 is connected to the main inlet 22 of the second compressor 20, and the MP outlet 5 of the refrigeration circuit 1 is connected to one of the side inlets 23 (lower pressure side) of the second compressor 20. The HP outlet 4 of the refrigeration circuit 1 is connected to the two main inlets 12 and 13 of the first compressor 10, and the HHP outlet 3 of the refrigeration circuit 1 is connected to the other side inlet 24 (higher pressure side) of the second compressor 20. The outlet 11 of the first compressor 10 and the outlet 21 of the second compressor 20 are both connected to the inlet 2 of the refrigeration circuit 1.
[0062] Fig. 11 shows an eleventh embodiment of the apparatus for compressing gaseous refrigerant according to the present invention. The apparatus of the eleventh embodiment comprises a first compressor 10 having a double suction configuration and a second compressor 20 having a straight suction configuration. The first compressor 10 includes a pair of main inlets 12 and 13 defined on either axial end of the casing and an outlet 11 defined in an axially middle part of the casing. In this case, the two parts of the dual suction configuration of the first compressor 10 may be either symmetric or asymmetric depending on different design considerations. Each set of impellers may
WO 2015/011742
PCT/JP2013/004568 include any number of impeller disks which are typically supported by a common shaft.
[0063] The second compressor 20 includes a plurality of impeller disks arranged in series along the axial length thereof. The casing of the second compressor 20 defines an outlet 21 at an axial end thereof, a main inlet 22 at the other axial end thereof and a single side inlet 23 in an axially intermediate position thereof. The two compressors 10 and 20 are driven by an output shaft 31 of a common gas turbine driver 30.
[0064] The LP outlet 6 of the refrigeration circuit 1 is connected to one of the main inlets 12 of the first compressor 10, and the MP outlet 4 of the refrigeration circuit 1 is connected to the other main inlet 13 of the first compressor 10. The HP outlet 4 of the refrigeration circuit 1 is connected to the main inlet 22 of the second compressor 20, and the HHP outlet 3 of the refrigeration circuit 1 is connected to the side inlet 23 of the second compressor 20. The outlet 11 of the first compressor 10 and the outlet 21 of the second compressor 20 are both connected to the inlet 2 of the refrigeration circuit 1.
[0065] Fig. 12 shows a twelfth embodiment of the apparatus for compressing gaseous refrigerant according to the present invention. The apparatus of the twelfth embodiment comprises a first compressor 10 having a double suction configuration and a second compressor 20 also having a double suction configuration. The first compressor 10 includes a pair of main inlets 12 and 13 defined on either axial end of the casing and an outlet 11 defined in an axially middle part of the casing. In this case, the two parts of the dual suction configuration of the first compressor 10 may be either symmetric or asymmetric depending on different design considerations. Each set of impellers may include any number of impeller disks which are typically supported by a common shaft.
[0066] The second compressor 20 also includes a pair of main inlets 22 and 23 defined on either axial end of the casing, a pair of side inlets 24 and 25 and an outlet 21 defined in an axially middle part of the casing. In this case, the two parts of the dual suction configuration of the second compressor 20 are preferably symmetric to each other. Each set of impellers may include any number of impeller disks which are typically supported by a common shaft. The two compressors 10 and 20 are driven by an output shaft 31 of a common gas turbine driver 30.
[0067] The LP outlet 6 of the refrigeration circuit 1 is connected to one of the two main inlets 12 of the first compressor 10, and the MP outlet 5 of the refrigeration circuit 1 is connected to the other main inlet 13 of the first compressor. The HP outlet 4 of the refrigeration circuit 1 is connected to the main inlets 22 and 23 of the second compressor 20, and the HHP outlet 3 of the refrigeration circuit 1 is connected to the two side inlets 24 and 25 of the second compressor 20. The outlet 11 of the first compressor 10
WO 2015/011742
PCT/JP2013/004568 and the outlet 21 of the second compressor 20 are both connected to the inlet 2 of the refrigeration circuit 1.
[0068] Fig. 13 shows a thirteenth embodiment of the apparatus for compressing gaseous refrigerant according to the present invention. The apparatus of the thirteenth embodiment comprises a first compressor 10 having a double suction configuration and a second compressor 20 also having a double suction configuration. The first compressor 10 includes a pair of main inlets 12 and 13 defined on either axial end of the casing and an outlet 11 defined in an axially middle part of the casing. In this case, the two parts of the dual suction configuration of the first compressor 10 may be either symmetric or asymmetric depending on different design considerations. Each set of impellers may include any number of impeller disks which are typically supported by a common shaft.
[0069] The second compressor 20 also includes a pair of main inlets 22 and 23 defined on either axial end of the casing and an outlet 21 defined in an axially middle part of the casing. In this case also, the two parts of the dual suction configuration of the first compressor 10 may be either symmetric or asymmetric depending on different design considerations. Each set of impellers may include any number of impeller disks which are typically supported by a common shaft. The two compressors 10 and 20 are driven by an output shaft 31 of a common gas turbine driver 30.
[0070] The LP outlet 6 of the refrigeration circuit 1 is connected to one of the two main inlets 12 of the first compressor 10, and the MP outlet 5 of the refrigeration circuit 1 is connected to the other main inlet 12 of the first compressor 10. The HP outlet 4 of the refrigeration circuit 1 is connected to one of the two main inlets 22 of the first compressor 20, and the HHP outlet 3 of the refrigeration circuit 1 is connected to the other main inlet 23 of the second compressor 20. The outlet 11 of the first compressor 10 and the outlet 21 of the second compressor 20 are both connected to the inlet 2 of the refrigeration circuit 1.
[0071] Fig. 14 shows a fourteenth embodiment of the apparatus for compressing gaseous refrigerant according to the present invention. The apparatus of the fourteenth embodiment comprises a first compressor 10 having a double suction configuration and a second compressor 20 having a straight suction configuration. The first compressor 10 includes a pair of main inlets 12 and 13 defined on either axial end of the casing and an outlet 11 defined in an axially middle part of the casing. In this case, the two parts of the dual suction configuration of the first compressor 10 may be either symmetric or asymmetric depending on different design considerations. Each set of impellers may include any number of impeller disks which are typically supported by a common shaft.
[0072] The second compressor 20 includes a plurality of impeller disks arranged in series
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PCT/JP2013/004568 along the axial length thereof. The casing of the second compressor 20 defines an outlet 21 at an axial end thereof, a main inlet 22 at the other axial end thereof and a single side inlet 23 in an axially intermediate position thereof. The two compressors 10 and 20 are driven by an output shaft 31 of a common gas turbine driver 30.
[0073] The LP outlet 6 of the refrigeration circuit 1 is connected to the main inlet 22 of the second compressor 20, and the MP outlet 4 of the refrigeration circuit 1 is connected to one of the main inlets 12 of the first compressor 10. The HP outlet 4 of the refrigeration circuit 1 is connected to the other main inlet 13 of the first compressor 10, and the HHP outlet 3 of the refrigeration circuit 1 is connected to the side inlet 23 of the second compressor 20. The outlet 11 of the first compressor and the outlet 21 of the second compressor 20 are both connected to the inlet 2 of the refrigeration circuit 1.
[0074] Fig. 15 shows a fifteenth embodiment of the apparatus for compressing gaseous refrigerant according to the present invention. The apparatus of the fifteenth embodiment comprises a first compressor 10 having a double suction configuration and a second compressor 20 also having a double suction configuration. The first compressor 10 includes a pair of main inlets 12 and 13 defined on either axial end of the casing and an outlet 11 defined in an axially middle part of the casing. In this case, the two parts of the dual suction configuration of the first compressor 10 may be either symmetric or asymmetric depending on different design considerations. Each set of impellers may include any number of impeller disks which are typically supported by a common shaft.
[0075] The second compressor 20 also includes a pair of main inlets 22 and 23 defined on either axial end of the casing, a pair of side inlets 24 and 25, and an outlet 21 defined in an axially middle part of the casing. In this case, the two parts of the dual suction configuration of the second compressor 20 are preferably symmetric to each other. Each set of impellers may include any number of impeller disks which are typically supported by a common shaft. The two compressors 10 and 20 are driven by an output shaft 31 of a common gas turbine driver 30.
[0076] The FP outlet 6 of the refrigeration circuit 1 is connected to the two main inlets 22 and 23 of the second compressor 20, and the MP outlet 5 of the refrigeration circuit 1 is connected to one of the main inlet 12 of the first compressor. The HP outlet 4 of the refrigeration circuit 1 is connected to the other main inlet 13 of the first compressor 10, and the HHP outlet 3 of the refrigeration circuit 1 is connected to the two side inlets 24 and 25 of the second compressor 20. The outlet 11 of the first compressor 10 and the outlet 21 of the second compressor 20 are both connected to the inlet 2 of the refrigeration circuit 1.
[0077] Fig. 16 shows a sixteenth embodiment of the apparatus for compressing gaseous refrigerant according to the present invention. The apparatus of the sixteenth em15
WO 2015/011742
PCT/JP2013/004568 bodiment comprises a first compressor 10 having a double suction configuration and a second compressor 20 having a straight suction configuration. The first compressor 10 includes a pair of main inlets 12 and 13 defined on either axial end of the casing and an outlet 11 defined in an axially middle part of the casing. In this case, the two parts of the dual suction configuration of the first compressor 10 may be either symmetric or asymmetric depending on different design considerations. Each set of impellers may include any number of impeller disks which are typically supported by a common shaft.
[0078] The second compressor 20 includes a plurality of impeller disks arranged in series along the axial length thereof. The casing of the second compressor 20 defines an outlet 21 at an axial end thereof, a main inlet 22 at the other axial end thereof and a single side inlet 23 in an axially intermediate position thereof. The two compressors 10 and 20 are driven by an output shaft 31 of a common gas turbine driver 30.
[0079] The LP outlet 6 of the refrigeration circuit 1 is connected to one of the main inlets 12 of the first compressor 10, and the MP outlet 4 of the refrigeration circuit 1 is connected to the main inlet 22 of the second compressor 20. The HP outlet 4 of the refrigeration circuit 1 is connected to the side inlet 23 of the second compressor 20, and the HHP outlet 3 of the refrigeration circuit 1 is connected to the other main inlet 13 of the first compressor 10. The outlet 11 of the first compressor 10 and the outlet 21 of the second compressor 20 are both connected to the inlet 2 of the refrigeration circuit 1.
[0080] Fig. 17 shows a seventeenth embodiment of the apparatus for compressing gaseous refrigerant according to the present invention. The apparatus of the seventeenth embodiment comprises a first compressor 10 having a double suction configuration and a second compressor 20 also having a double suction configuration. The first compressor 10 includes a pair of main inlets 12 and 13 defined on either axial end of the casing and an outlet 11 defined in an axially middle part of the casing. In this case, the two parts of the dual suction configuration of the first compressor 10 may be either symmetric or asymmetric depending on different design considerations. Each set of impellers may include any number of impeller disks which are typically supported by a common shaft.
[0081] The second compressor 20 also includes a pair of main inlets 22 and 23 defined on either axial end of the casing, a pair of side inlets 24 and 25 and an outlet 21 defined in an axially middle part of the casing. In this case, the two parts of the dual suction configuration of the second compressor 20 are preferably symmetric to each other. Each set of impellers may include any number of impeller disks which are typically supported by a common shaft. The two compressors 10 and 20 are driven by an output shaft 31 of a common gas turbine driver 30.
WO 2015/011742 PCT/JP2013/004568 [0082] The LP outlet 6 of the refrigeration circuit 1 is connected to one of the two main inlets 12 of the first compressor 10, and the MP outlet 5 of the refrigeration circuit 1 is connected to the main inlets 22 and 23 of the second compressor 20. The HP outlet 4 of the refrigeration circuit 1 is connected to the two side inlets 24 and 25 of the second compressor 20, and the HHP outlet 3 of the refrigeration circuit 1 is connected to the other main inlet 13 of the first compressor 10. The outlet 11 of the first compressor 10 and the outlet 21 of the second compressor 20 are both connected to the inlet 2 of the refrigeration circuit 1.
[0083] Fig. 18 shows an eighteenth embodiment of the apparatus for compressing gaseous refrigerant according to the present invention. The apparatus of the eighteenth embodiment comprises a first compressor 10 having a double suction configuration and a second compressor 20 also having a double suction configuration. The first compressor 10 includes a pair of main inlets 12 and 13 defined on either axial end of the casing and an outlet 11 defined in an axially middle part of the casing. In this case, the two parts of the dual suction configuration of the first compressor 10 may be either symmetric or asymmetric depending on different design considerations. Each set of impellers may include any number of impeller disks which are typically supported by a common shaft.
[0084] The second compressor 20 also includes a pair of main inlets 22 and 23 defined on either axial end of the casing and an outlet 21 defined in an axially middle part of the casing. In this case, the two parts of the dual suction configuration of the first compressor 10 may be either symmetric or asymmetric depending on different design considerations. Each set of impellers may include any number of impeller disks which are typically supported by a common shaft. The two compressors 10 and 20 are driven by an output shaft 31 of a common gas turbine driver 30.
[0085] The FP outlet 6 of the refrigeration circuit 1 is connected to one of the two main inlets 12 of the first compressor 10, and the MP outlet 5 of the refrigeration circuit 1 is connected to one of the two main inlets 22 of the second compressor 20. The HP outlet 4 of the refrigeration circuit 1 is connected to the other main inlet 23 of the second compressor 20, and the HHP outlet 3 of the refrigeration circuit 1 is connected to the other main inlet 12 of the first compressor 10. The outlet 11 of the first compressor 10 is connected to the inlet 2 of the refrigeration circuit 1. Fikewise, the outlet 21 of the second compressor 120 is connected to the inlet 2 of the refrigeration circuit 1.
[0086] Fig. 19 shows a nineteenth embodiment of the apparatus for compressing gaseous refrigerant according to the present invention. The apparatus of the nineteenth embodiment comprises a first compressor 10 having a double suction configuration and a second compressor 20 having a straight suction configuration. The first compressor 10 includes a pair of main inlets 12 and 13 defined on either axial end of the casing and an
WO 2015/011742
PCT/JP2013/004568 outlet 11 defined in an axially middle part of the casing. In this case, the two parts of the dual suction configuration of the first compressor 10 may be either symmetric or asymmetric depending on different design considerations. Each set of impellers may include any number of impeller disks which are typically supported by a common shaft.
[0087] The second compressor 20 includes a plurality of impeller disks arranged in series along the axial length thereof. The casing of the second compressor 20 defines an outlet 21 at an axial end thereof, a main inlet 22 at the other axial end thereof and a single side inlet 23 in an axially intermediate position thereof. The two compressors 10 and 20 are driven by an output shaft 31 of a common gas turbine driver 30.
[0088] The LP outlet 6 of the refrigeration circuit 1 is connected to one of the main inlets 12 of the first compressor 10, and the MP outlet 4 of the refrigeration circuit 1 is connected to the main inlet 22 of the second compressor 20. The HP outlet 4 of the refrigeration circuit 1 is connected to the other main inlet 13 of the first compressor 10, and the HHP outlet 3 of the refrigeration circuit 1 is connected to the side inlet 23 of the second compressor 20. The outlet 11 of the first compressor 10 and the outlet 21 of the second compressor 20 are both connected to the inlet 2 of the refrigeration circuit
1.
[0089] Fig. 20 shows a twentieth embodiment of the apparatus for compressing gaseous refrigerant according to the present invention. The apparatus of the twentieth embodiment comprises a first compressor 10 having a double suction configuration and a second compressor 20 also having a double suction configuration. The first compressor 10 includes a pair of main inlets 12 and 13 defined on either axial end of the casing and an outlet 11 defined in an axially middle part of the casing. In this case, the two parts of the dual suction configuration of the first compressor 10 may be either symmetric or asymmetric depending on different design considerations. Each set of impellers may include any number of impeller disks which are typically supported by a common shaft.
[0090] The second compressor 20 also includes a pair of main inlets 22 and 23 defined on either axial end of the casing and an outlet 21 defined in an axially middle part of the casing. In this case also, the two parts of the dual suction configuration of the first compressor 10 may be either symmetric or asymmetric depending on different design considerations. Each set of impellers may include any number of impeller disks which are typically supported by a common shaft. The two compressors 10 and 20 are driven by an output shaft 31 of a common gas turbine driver 30.
[0091] The FP outlet 6 of the refrigeration circuit 1 is connected to one of the two main inlets 12 of the first compressor 10, and the MP outlet 5 of the refrigeration circuit 1 is connected to one of the two main inlets 22 of the second compressor 20. The HP outlet
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PCT/JP2013/004568 of the refrigeration circuit 1 is connected to the other main inlet 12 of the first compressor 10, and the HHP outlet 3 of the refrigeration circuit 1 is connected to the other main inlet 23 of the second compressor 20. The outlet 11 of the first compressor and the outlet 21 of the second compressor 20 are both connected to the inlet 2 of the refrigeration circuit 1.
[0092] The present invention can be implemented in a number of different ways as discussed above. In the foregoing embodiments, the refrigeration circuit 1 included four outlets LP, MP, HP and HHP which are denoted with numerals 6, 5, 4, 3 and 2, re spectively. Using notations A, D and S to denote asymmetric double suction configuration , symmetric double suction configuration and straight suction configuration in combination with the associated outlets 6, 5, 4, 3 and 2 of the refrigeration circuit 1, each of the illustrated embodiments can be designated by the following notations.
Embodiment Drawing Notation
1 Figs, la and lb D6-S543
2 Figs.2a and 2b D54-S63
3 Fig. 3 D65-S43
4 Fig.4 D65-D43
5 Fig. 5 D63-D54
6 Fig.6 D64-D53
7 Fig. 7 D64-S53
8 Fig.8 D63-S54
9 Fig.9 D5-S643
10 Fig. 10 D4S653
11 Fig.11 A65-S43
12 Fig. 12 A65-D43
13 Fig. 13 A65-A43
14 Fig. 14 A54-S63
15 Fig.15 A54-D63
16 Fig.16 A63-S54
17 Fig. 17 A63-D54
18 Fig. 18 A63-A54
19 Fig. 19 A64-S53
20 Fig. 20 A64-A53
These notations are helpful in sorting out different combinations of the compressors and the connections between the compressors and the refrigeration circuit. Also, by using these notations, it is also possible to consider different other combinations of the compressors and the connections between the compressors and the refrigeration circuit. Such other combinations which are not covered by the foregoing embodiments are also part of the present invention.
[0093] Although the present invention has been described in terms of preferred embodiments thereof, it is obvious to a person skilled in the art that various alterations and modifications are possible without departing from the scope of the present invention which is set forth in the appended claims. The contents of the prior art
2013395108 19 Jan 2018
- 19references mentioned in this application are incorporated in this application by reference.
[0094] Throughout the specification and the claims that follow, unless the context requires otherwise, the words “comprise” and “include” and variations such as “comprising” and “including” will be understood to imply the inclusion of a stated integer or group of integers, but not the exclusion of any other integer or group of integers.
[0095] The reference to any prior art in this specification is not, and should not be taken as, an acknowledgement of any form of suggestion that such prior art forms part of the common general knowledge.
2013395108 03 Jul 2018

Claims (13)

  1. THE CLAIMS DEFINING THE INVENTION ARE AS FOLLOWS:
    1. Apparatus for compressing gaseous refrigerant for use in a refrigeration circuit of a liquefaction plant, the apparatus comprising:
    a refrigeration circuit including an inlet for refrigerant at a refrigeration pressure, a low pressure outlet for gaseous refrigerant at a low pressure, a high pressure outlet for gaseous refrigerant at a high pressure and at least one intermediate pressure outlet for gaseous refrigerant at an intermediate pressure;
    a first compressor received in a first casing and provided with a double suction configuration including at least two main inlets defined on either axial ends of the casing and one outlet defined in an axially middle part of the casing;
    a second compressor received in a second casing separate from the first casing and having an at least one main inlet, a first side inlet, a second side inlet for a higher pressure input than the first side inlet, and an outlet; and a common power source including an output shaft for driving the first and second compressors;
    wherein the outlet of the first compressor is connected to the second side inlet of the second compressor, and the outlet of the second compressor is connected to the inlet of the refrigeration circuit; and wherein the low pressure outlet of the refrigeration circuit is connected to the main inlets of the first compressor, the at least one intermediate pressure outlet of the refrigeration circuit is connected to the main inlet of the second compressor, and the high pressure outlet of the refrigeration circuit is connected to the first side inlet of the second compressor.
  2. 2. The apparatus according to claim 1, wherein the second compressor is further provided with a third side inlet, the third inlet being connected to another of the intermediate pressure outlets of the refrigeration circuit.
  3. 3. The apparatus according to claim 1, wherein the first compressor is further provided with a pair of side inlets in a symmetric configuration that are connected to another of the intermediate pressure outlets of the refrigeration circuit.
  4. 4. The apparatus according to claim 1, wherein the first compressor has no side inlets.
  5. 5. The apparatus according to claim 1, wherein the second compressor is provided with a straight suction configuration.
    -21 2013395108 03 Jul 2018
  6. 6. The apparatus according to claim 5, wherein the outlet of the second compressor is connected to the inlet of the refrigeration circuit via an economizer.
  7. 7. The apparatus according to claim 1, wherein the second compressor is provided with a double suction configuration.
  8. 8. The apparatus according to claim 1, wherein the refrigeration circuit comprises two intermediate pressure outlets for gaseous refrigerant at intermediate pressures.
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AU2013395108A 2013-07-26 2013-07-26 Refrigeration compression system using two compressors Ceased AU2013395108B2 (en)

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IT201600080745A1 (en) * 2016-08-01 2018-02-01 Nuovo Pignone Tecnologie Srl REFRIGERANT COMPRESSOR DIVIDED FOR NATURAL GAS LIQUEFATION
US10544986B2 (en) 2017-03-29 2020-01-28 Air Products And Chemicals, Inc. Parallel compression in LNG plants using a double flow compressor

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AP2015008918A0 (en) 2015-12-31
US20160131422A1 (en) 2016-05-12

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