US20110094251A1 - Dual turbo centrifugal chiller - Google Patents

Dual turbo centrifugal chiller Download PDF

Info

Publication number
US20110094251A1
US20110094251A1 US12/796,014 US79601410A US2011094251A1 US 20110094251 A1 US20110094251 A1 US 20110094251A1 US 79601410 A US79601410 A US 79601410A US 2011094251 A1 US2011094251 A1 US 2011094251A1
Authority
US
United States
Prior art keywords
compressor
evaporator
condenser
compressors
impellers
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
Application number
US12/796,014
Inventor
Kil Young Kim
Jin Sung Kim
Tae Jin Kang
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
LG Electronics Inc
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Assigned to LS MTRON LTD. reassignment LS MTRON LTD. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: KANG, TAE JIN, KIM, JIN SUNG, KIM, KIL YOUNG
Publication of US20110094251A1 publication Critical patent/US20110094251A1/en
Assigned to LG ELECTRONICS INC. reassignment LG ELECTRONICS INC. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: LS MTRON, LTD.
Abandoned legal-status Critical Current

Links

Images

Classifications

    • 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
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B1/00Compression machines, plants or systems with non-reversible cycle
    • F25B1/04Compression machines, plants or systems with non-reversible cycle with compressor of rotary type
    • F25B1/053Compression machines, plants or systems with non-reversible cycle with compressor of rotary type of turbine type
    • 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
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B7/00Compression machines, plants or systems, with cascade operation, i.e. with two or more circuits, the heat from the condenser of one circuit being absorbed by the evaporator of the next circuit
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04DNON-POSITIVE-DISPLACEMENT PUMPS
    • F04D27/00Control, e.g. regulation, of pumps, pumping installations or pumping systems specially adapted for elastic fluids
    • 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
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B1/00Compression machines, plants or systems with non-reversible cycle
    • F25B1/10Compression machines, plants or systems with non-reversible cycle with multi-stage compression
    • 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
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B5/00Compression machines, plants or systems, with several evaporator circuits, e.g. for varying refrigerating capacity
    • 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
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B6/00Compression machines, plants or systems, with several condenser circuits
    • 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
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2339/00Details of evaporators; Details of condensers
    • F25B2339/04Details of condensers
    • F25B2339/047Water-cooled condensers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2400/00General 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
    • F25B2400/07Details of compressors or related parts
    • F25B2400/075Details of compressors or related parts with parallel compressors
    • F25B2400/0751Details of compressors or related parts with parallel compressors the compressors having different capacities

Definitions

  • This disclosure relates to a dual turbo centrifugal chiller, particularly to a dual turbo centrifugal chiller configured to decrease head of a compressor among components of two individual chillers, decrease the size of the chiller, and increase efficiency.
  • a general chiller includes a compressor, an evaporator, a condenser, and an expansion valve, and circulates a refrigerant to transfer heat from the evaporator to the condenser through heat exchange.
  • FIG. 1 is a diagram schematically illustrating a general chiller 10 .
  • the chiller 10 includes an evaporator 30 , a condenser 20 , and a compressor 40 .
  • Cold water 31 flows through the evaporator 30
  • cooling water 21 flow through the condenser 20 .
  • the compressor 40 in which a refrigerant 51 , 52 is circulated connects the evaporator 30 to the condenser 20 .
  • the refrigerant 51 that passes through the evaporator 30 flows into the compressor 40 through an inlet portion 47 of the compressor 40 , and the refrigerant 52 compressed by two-stage impellers 41 and 42 flows out of an outlet portion 48 of the compressor 40 and then flows into the condenser 20 .
  • the two-stage impellers 41 and 42 are provided on a shaft 43 , and the impellers 41 and 42 are rotated as the shaft 43 is rotated by a motor 45 .
  • gears 44 and 46 are provided to connect the motor 45 to the shaft 43 so as to transmit torque.
  • a thrust bearing may be connected between the gear 44 and the shaft 43 .
  • a load applied to the bearing increases because a thrust that is transferred to the gears 46 and 44 is focused in one direction, and, thus, a load applied to the motor 45 also increases.
  • a load applied to the motor 45 increases, an outlet temperature of the cold water increases, which results in an increase in head of the compressor. As a result, the efficiency of the compressor is decreased.
  • a ‘dual turbo centrifugal chiller’ which includes two chillers connected to each other has been used.
  • the dual turbo centrifugal chiller has an increased capacity by increasing the chilling efficiency of the chiller itself.
  • two compressors are provided.
  • one of the two compressors has a higher head than the other. Therefore, the two compressors have to be independently designed and manufactured. That is, a driving unit for driving an impeller of each of the compressors is additionally needed, and the entire size of the chiller is increased. Accordingly, as described above, there is a problem in that the efficiency of the compressor is decreased.
  • This disclosure provides a dual turbo centrifugal chiller in which two compressors, two evaporators, and two condensers are included to decrease heads of the compressors, the compressors are configured to operate with the same head, and impellers of the compressors are driven by a single driving unit, thereby achieving a decrease in size and an increase in efficiency.
  • a dual turbo centrifugal chiller including: first and second evaporators connected in series or in parallel; first and second condensers connected in series or in parallel; and first and second compressors including impellers, wherein cold water passes through the second evaporator after passing through the first evaporator, and cooling water passes through the second condenser after passing through the first condenser, the first compressor containing a refrigerant connects the first condenser to the second evaporator, and the second compressor containing a refrigerant connects the second condenser to the first evaporator, and the impellers of the first compressor and the second compressor are rotated simultaneously using a single driving unit.
  • impellers of the first and second compressors may be connected with a single rotation shaft, and the impellers of the first and second compressors may be rotated simultaneously as the rotation shaft is rotated using the driving unit.
  • the driving unit may be connected to the center of the rotation shaft, and the impellers of the first and second compressors may be opposed with the center of the rotation shaft between them.
  • inlet portions of the first and second compressors may be provided with inlet guide vanes (IGVs) respectively.
  • IGVs inlet guide vanes
  • first and second compressors may have different capacities from each other.
  • the dual turbo centrifugal chiller including the two evaporators, the two compressors and the two condensers maintains the reduced head of each compressor, it is possible to achieve the optimal performance of the compressor.
  • FIG. 1 is a diagram schematically illustrating a general chiller
  • FIG. 2 is a diagram schematically illustrating a dual turbo centrifugal chiller according to an embodiment
  • FIG. 3 is a diagram schematically illustrating a dual turbo centrifugal chiller according to another embodiment.
  • FIG. 2 is a diagram schematically illustrating a dual turbo centrifugal chiller 101 according to an embodiment.
  • a first evaporator 121 and a second evaporator 122 are connected in series.
  • Cold water 123 flows into an end of the first evaporator 121 connected in series, passes through the first evaporator 121 , passes through the second evaporator 122 , and then flows out.
  • a first condenser 111 and a second condenser 112 are connected in series. Cooling water 113 passes through the first condenser 111 , flows into the second condenser 112 , passes through the second condenser 112 , and then flows out.
  • a first compressor 131 is connected to the first condenser 111 and the second evaporator 122 such that a refrigerant of the first compressor 131 is circulated to exchange heat with the cooling water 113 of the first condenser 111 and the cold water 123 of the second evaporator 122 .
  • a second compressor 132 is connected to the second condenser 112 and the first evaporator 121 such that a refrigerant of the second compressor 132 is circulated to exchange heat with the cooling water 113 of the second compressor 112 and the cold water 123 of the first evaporator 121 .
  • a temperature of the cold water that flows into the first evaporator 121 is 12° C.
  • a temperature of the cold water that flows out of the second evaporator 122 is 7° C.
  • a temperature of the cooling water that flows into the first condenser 111 is 32° C.
  • a temperature of the cooling water that flows out of the second condenser 112 is 37° C.
  • a head of the first compressor 131 is 27.5° C. (34.5° C.-7° C.), and a head of the second compressor 132 is also 27.5° C. (37° C.-9.5° C.).
  • the heads of the two compressors 131 and 132 are equal to each other. Accordingly, as described below, a design for simultaneously driving impellers of the two compressors using a single driving unit may be easily achieved.
  • the first compressor 131 is a two-stage compression system having two impellers 145 and 146 .
  • a refrigerant 151 flows out of the second evaporator 122 into the first compressor 131 through an inlet portion 141 of the first compressor 131 , and the refrigerant is compressed while passing through the impellers 145 and 146 .
  • the compressed refrigerant 152 flows out of the first compressor 131 through an outlet portion 142 and flows into the first condenser 111 .
  • the second compressor 132 is a two-stage compression system having two impellers 143 and 144 .
  • a refrigerant 153 that flows out of the first evaporator 121 flows into the second compressor 132 through an inlet portion 143 of the second compressor 132 , and the refrigerant is compressed while passing through the impellers 143 and 144 .
  • the compressed refrigerant 154 flows out of the second compressor 132 through an outlet portion 144 and flows into the second condenser 122 .
  • a single driving unit 163 for rotating the impellers 143 , 144 , 145 , and 146 of the two compressors 131 and 132 is provided.
  • an electric motor is used as the driving unit 163 .
  • the impellers 143 , 144 , 145 , and 146 of the two compressors 131 and 132 are connected with a rotation shaft 161 .
  • a gear 162 is provided at the center of the rotation shaft 161 , the impellers 145 and 146 of the first compressor 131 and the impellers 143 and 144 of the second compressor 132 are opposed with the center of the rotation shaft 161 between them.
  • An end portion of the driving unit 163 is connected to a gear, and the gear connected to the driving unit 163 is engaged with a gear 162 of the rotation shaft 161 .
  • the single driving unit 163 rotates the rotation shaft 161 , and as the rotation shaft 161 is rotated, the impellers 143 , 144 , 145 , and 146 of the two compressors 131 and 132 are rotated simultaneously.
  • the two individual compressors 131 and 132 are driven by the single driving unit 163 , the entire volume of the compressor system is reduced. Therefore, the entire size of the dual turbo centrifugal chiller 101 is reduced.
  • the inlet portions of the first and second compressors 131 and 132 are provided with inlet guide vanes (IGVs) for adjusting loads applied thereto in order to facilitate load adjustment.
  • IGVs inlet guide vanes
  • the first and second compressors 131 and 132 are separated from each other, various combinations of capacity may be attained with the compressors and the heat exchangers (the condensers and the evaporators).
  • the capacities of the compressors 131 and 132 may be set to 1,000 RT and 500 RT, respectively.
  • the size of the heat exchanger is determined according to the capacity of the compressor. Even in this case, the impellers of the compressors are disposed symmetrically on the single rotation shaft, and since the impellers are disposed symmetrically, the thrust cancellation effect of the bearing is exhibited even in the case where the capacities of the two compressors are different from each other.
  • the two evaporators 121 and 122 are connected in series, and the two condensers 111 and 112 are connected in series, however, the embodiment is not limited to that configuration.
  • another embodiment will be described with reference to FIG. 3 .
  • FIG. 3 is a diagram schematically illustrating a dual turbo centrifugal chiller 201 according to another embodiment.
  • a first evaporator 221 and a second evaporator 222 are connected in parallel.
  • Cold water 223 flows into an end of the first evaporator 221 connected in parallel and flows out of the other end of the first evaporator 221 , flows into an end of the second evaporator 222 , passes through the second evaporator 222 , and flows out of the other end of the second evaporator 222 .
  • a first condenser 211 and a second condenser 212 are connected in parallel. Cooling water 213 flows into an end of the first condenser 211 connected in parallel, flows out of the other end of the first condenser 211 , flows into an end of the second condenser 212 , passes through the second condenser 212 , and flows out of the other end of the second condenser 212 .
  • a first compressor 231 is connected to the first condenser 211 and the second evaporator 222 , and a refrigerant of the first compressor 231 is circulated to exchange heat with the cooling water of the first condenser 211 and the cold water of the second evaporator 222 .
  • a second compressor 232 is connected to the second condenser 212 and the first evaporator 221 , and a refrigerant of the second compressor 232 is circulated to exchange heat with the cooling water of the second condenser 212 and the cold water of the first evaporator 221 .
  • a temperature of the cold water that flows into the first evaporator 221 is 12° C.
  • a temperature of the cold water that flows out of the second evaporator 222 is 7° C.
  • a temperature of the cooling water that flows into the first condenser 211 is 32° C.
  • a temperature of the cooling water that flows out of the second condenser 212 is 37° C.
  • a head of the first compressor 231 is 27.5° C. (34.5° C.-7° C.), and a head of the second compressor 232 is also 27.5° C. (37° C.-9.5° C.). That is, the heads of the two compressors are equal to each other.
  • connection relationships between impellers 245 , 246 , 247 , and 248 of the compressors 231 and 232 , the rotation shaft 161 , a gear 262 , and a driving unit 263 provided in the dual turbo centrifugal chiller 201 according to this embodiment, and a flow of a refrigerant 251 , 252 , 253 , and 254 at inlet and outlet portions 243 and 244 of the compressor are the same as those of the embodiment illustrated in FIG. 2 , a detailed description thereof will be omitted.
  • the two evaporators may be connected in serial or in parallel, and the two condensers may be connected in serial or in parallel.
  • cold water passes through a first evaporator and a second evaporator
  • cooling water passes through a second condenser after passing through a first condenser
  • a first compressor containing a refrigerant is connected to the first condenser and the second evaporator
  • a second compressor containing a refrigerant is connected to the second condenser and the first evaporator

Landscapes

  • 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 dual turbo centrifugal chiller includes: first and second evaporators connected in series or in parallel; first and second condensers connected in series or in parallel; and first and second compressors including impellers, wherein cold water passes through the second evaporator after passing through the first evaporator, and cooling water passes through the second condenser after passing through the first condenser, the first compressor containing a refrigerant connects the first condenser to the second evaporator, and the second compressor containing a refrigerant connects the second condenser to the first evaporator, and the impellers of the first compressor and second compressor are rotated simultaneously using a single driving unit.

Description

    CROSS-REFERENCE TO RELATED APPLICATION
  • This application claims priority to Korean Patent Application No. 10-2009-0102209, filed on Oct. 27, 2009, and all the benefits accruing therefrom under 35 U.S.C. §119, the contents of which in its entirety are herein incorporated by reference.
  • BACKGROUND
  • 1. Field
  • This disclosure relates to a dual turbo centrifugal chiller, particularly to a dual turbo centrifugal chiller configured to decrease head of a compressor among components of two individual chillers, decrease the size of the chiller, and increase efficiency.
  • 2. Description of the Related Art
  • A general chiller includes a compressor, an evaporator, a condenser, and an expansion valve, and circulates a refrigerant to transfer heat from the evaporator to the condenser through heat exchange.
  • FIG. 1 is a diagram schematically illustrating a general chiller 10.
  • As illustrated in FIG. 1, the chiller 10 includes an evaporator 30, a condenser 20, and a compressor 40. Cold water 31 flows through the evaporator 30, and cooling water 21 flow through the condenser 20.
  • The compressor 40 in which a refrigerant 51, 52 is circulated connects the evaporator 30 to the condenser 20. The refrigerant 51 that passes through the evaporator 30 flows into the compressor 40 through an inlet portion 47 of the compressor 40, and the refrigerant 52 compressed by two- stage impellers 41 and 42 flows out of an outlet portion 48 of the compressor 40 and then flows into the condenser 20.
  • As illustrated in FIG. 1, in the compressor 40, the two- stage impellers 41 and 42 are provided on a shaft 43, and the impellers 41 and 42 are rotated as the shaft 43 is rotated by a motor 45. Here, gears 44 and 46 are provided to connect the motor 45 to the shaft 43 so as to transmit torque. Although not shown in the figure, a thrust bearing may be connected between the gear 44 and the shaft 43.
  • In the general compressor 40, a load applied to the bearing increases because a thrust that is transferred to the gears 46 and 44 is focused in one direction, and, thus, a load applied to the motor 45 also increases. As the load applied to the motor 45 increases, an outlet temperature of the cold water increases, which results in an increase in head of the compressor. As a result, the efficiency of the compressor is decreased.
  • In order to decrease the head of the compressor and increase the efficiency of the chiller, a ‘dual turbo centrifugal chiller’ which includes two chillers connected to each other has been used. The dual turbo centrifugal chiller has an increased capacity by increasing the chilling efficiency of the chiller itself. In the dual turbo centrifugal chiller, two compressors are provided. However, in the existing dual turbo centrifugal chiller, one of the two compressors has a higher head than the other. Therefore, the two compressors have to be independently designed and manufactured. That is, a driving unit for driving an impeller of each of the compressors is additionally needed, and the entire size of the chiller is increased. Accordingly, as described above, there is a problem in that the efficiency of the compressor is decreased.
  • SUMMARY
  • This disclosure provides a dual turbo centrifugal chiller in which two compressors, two evaporators, and two condensers are included to decrease heads of the compressors, the compressors are configured to operate with the same head, and impellers of the compressors are driven by a single driving unit, thereby achieving a decrease in size and an increase in efficiency.
  • In one aspect, there is a provided a dual turbo centrifugal chiller including: first and second evaporators connected in series or in parallel; first and second condensers connected in series or in parallel; and first and second compressors including impellers, wherein cold water passes through the second evaporator after passing through the first evaporator, and cooling water passes through the second condenser after passing through the first condenser, the first compressor containing a refrigerant connects the first condenser to the second evaporator, and the second compressor containing a refrigerant connects the second condenser to the first evaporator, and the impellers of the first compressor and the second compressor are rotated simultaneously using a single driving unit.
  • In addition, the impellers of the first and second compressors may be connected with a single rotation shaft, and the impellers of the first and second compressors may be rotated simultaneously as the rotation shaft is rotated using the driving unit.
  • In addition, the driving unit may be connected to the center of the rotation shaft, and the impellers of the first and second compressors may be opposed with the center of the rotation shaft between them.
  • In addition, inlet portions of the first and second compressors may be provided with inlet guide vanes (IGVs) respectively.
  • In addition, the first and second compressors may have different capacities from each other.
  • Since the dual turbo centrifugal chiller including the two evaporators, the two compressors and the two condensers maintains the reduced head of each compressor, it is possible to achieve the optimal performance of the compressor.
  • In addition, since the impellers of the two compressors are driven simultaneously using the single driving unit, it is possible to implement the compressor having a small size and high efficiency.
  • BRIEF DESCRIPTION OF THE DRAWINGS
  • The above and other aspects, features and advantages of the disclosed exemplary embodiments will be more apparent from the following detailed description taken in conjunction with the accompanying drawings in which:
  • FIG. 1 is a diagram schematically illustrating a general chiller;
  • FIG. 2 is a diagram schematically illustrating a dual turbo centrifugal chiller according to an embodiment; and
  • FIG. 3 is a diagram schematically illustrating a dual turbo centrifugal chiller according to another embodiment.
  • DETAILED DESCRIPTION
  • Exemplary embodiments now will be described more fully hereinafter with reference to the accompanying drawings, in which exemplary embodiments are shown. This disclosure may, however, be embodied in many different forms and should not be construed as limited to the exemplary embodiments set forth therein. Rather, these exemplary embodiments are provided so that this disclosure will be thorough and complete, and will fully convey the scope of this disclosure to those skilled in the art. In the description, details of well-known features and techniques may be omitted to avoid unnecessarily obscuring the presented embodiments.
  • The terminology used herein is for the purpose of describing particular embodiments only and is not intended to be limiting of this disclosure. As used herein, the singular forms “a”, “an” and “the” are intended to include the plural forms as well, unless the context clearly indicates otherwise. Furthermore, the use of the terms a, an, etc. does not denote a limitation of quantity, but rather denotes the presence of at least one of the referenced item. It will be further understood that the terms “comprises” and/or “comprising”, or “includes” and/or “including” when used in this specification, specify the presence of stated features, regions, integers, steps, operations, elements, and/or components, but do not preclude the presence or addition of one or more other features, regions, integers, steps, operations, elements, components, and/or groups thereof.
  • Unless otherwise defined, all terms (including technical and scientific terms) used herein have the same meaning as commonly understood by one of ordinary skill in the art. It will be further understood that terms, such as those defined in commonly used dictionaries, should be interpreted as having a meaning that is consistent with their meaning in the context of the relevant art and the present disclosure, and will not be interpreted in an idealized or overly formal sense unless expressly so defined herein.
  • In the drawings, like reference numerals in the drawings denote like elements. The shape, size and regions, and the like, of the drawing may be exaggerated for clarity.
  • FIG. 2 is a diagram schematically illustrating a dual turbo centrifugal chiller 101 according to an embodiment.
  • As illustrated in FIG. 2, according to the embodiment, a first evaporator 121 and a second evaporator 122 are connected in series. Cold water 123 flows into an end of the first evaporator 121 connected in series, passes through the first evaporator 121, passes through the second evaporator 122, and then flows out.
  • A first condenser 111 and a second condenser 112 are connected in series. Cooling water 113 passes through the first condenser 111, flows into the second condenser 112, passes through the second condenser 112, and then flows out.
  • A first compressor 131 is connected to the first condenser 111 and the second evaporator 122 such that a refrigerant of the first compressor 131 is circulated to exchange heat with the cooling water 113 of the first condenser 111 and the cold water 123 of the second evaporator 122. A second compressor 132 is connected to the second condenser 112 and the first evaporator 121 such that a refrigerant of the second compressor 132 is circulated to exchange heat with the cooling water 113 of the second compressor 112 and the cold water 123 of the first evaporator 121.
  • A temperature of the cold water that flows into the first evaporator 121 is 12° C., a temperature of the cold water that flows out of the second evaporator 122 is 7° C., a temperature of the cooling water that flows into the first condenser 111 is 32° C., and a temperature of the cooling water that flows out of the second condenser 112 is 37° C.
  • Without consideration of leaving temperature differences (LTDs) of the evaporator and the condenser, a head of the first compressor 131 is 27.5° C. (34.5° C.-7° C.), and a head of the second compressor 132 is also 27.5° C. (37° C.-9.5° C.).
  • In the dual turbo centrifugal chiller 101 according to the embodiment, as described above, the heads of the two compressors 131 and 132 are equal to each other. Accordingly, as described below, a design for simultaneously driving impellers of the two compressors using a single driving unit may be easily achieved.
  • Hereinafter, configurations of the two compressors 131 and 132 according to the embodiment will be described with reference to FIG. 2.
  • According to the embodiment, the first compressor 131 is a two-stage compression system having two impellers 145 and 146. A refrigerant 151 flows out of the second evaporator 122 into the first compressor 131 through an inlet portion 141 of the first compressor 131, and the refrigerant is compressed while passing through the impellers 145 and 146. The compressed refrigerant 152 flows out of the first compressor 131 through an outlet portion 142 and flows into the first condenser 111.
  • The second compressor 132 is a two-stage compression system having two impellers 143 and 144. A refrigerant 153 that flows out of the first evaporator 121 flows into the second compressor 132 through an inlet portion 143 of the second compressor 132, and the refrigerant is compressed while passing through the impellers 143 and 144. The compressed refrigerant 154 flows out of the second compressor 132 through an outlet portion 144 and flows into the second condenser 122.
  • According to the embodiment, a single driving unit 163 for rotating the impellers 143, 144, 145, and 146 of the two compressors 131 and 132 is provided. In this embodiment, an electric motor is used as the driving unit 163.
  • The impellers 143, 144, 145, and 146 of the two compressors 131 and 132 are connected with a rotation shaft 161. A gear 162 is provided at the center of the rotation shaft 161, the impellers 145 and 146 of the first compressor 131 and the impellers 143 and 144 of the second compressor 132 are opposed with the center of the rotation shaft 161 between them. An end portion of the driving unit 163 is connected to a gear, and the gear connected to the driving unit 163 is engaged with a gear 162 of the rotation shaft 161. In this configuration, the single driving unit 163 rotates the rotation shaft 161, and as the rotation shaft 161 is rotated, the impellers 143, 144, 145, and 146 of the two compressors 131 and 132 are rotated simultaneously.
  • According to the embodiment, since the two individual compressors 131 and 132 are driven by the single driving unit 163, the entire volume of the compressor system is reduced. Therefore, the entire size of the dual turbo centrifugal chiller 101 is reduced.
  • In addition, since the impellers of the two compressors are disposed symmetrically, thrusts applied to both ends of the gear 162 occur in the opposite direction and cancel each other out. Accordingly, a load applied to a bearing (not shown) used for the gear 162 decreases, which results in a decrease in the load applied to the driving unit 163 and an increase in the efficiency of the driving unit 163. The increase in the efficiency of the driving unit 163 causes a decrease in the outlet temperature of the cooling water, and this causes a decrease in the heads of the compressors 131 and 132. Accordingly, there are advantages in that the efficiency of the entire compression system increases, and the efficiency of the entire chiller increases. In addition, in designing the bearing, a design of the bearing without concern about the thrust applied in particular direction may be achieved.
  • According to the embodiment, the inlet portions of the first and second compressors 131 and 132 are provided with inlet guide vanes (IGVs) for adjusting loads applied thereto in order to facilitate load adjustment.
  • According to the embodiment, since the first and second compressors 131 and 132 are separated from each other, various combinations of capacity may be attained with the compressors and the heat exchangers (the condensers and the evaporators). For example, the capacities of the compressors 131 and 132 may be set to 1,000 RT and 500 RT, respectively. The size of the heat exchanger is determined according to the capacity of the compressor. Even in this case, the impellers of the compressors are disposed symmetrically on the single rotation shaft, and since the impellers are disposed symmetrically, the thrust cancellation effect of the bearing is exhibited even in the case where the capacities of the two compressors are different from each other.
  • In this embodiment, the two evaporators 121 and 122 are connected in series, and the two condensers 111 and 112 are connected in series, however, the embodiment is not limited to that configuration. Hereinafter, another embodiment will be described with reference to FIG. 3.
  • FIG. 3 is a diagram schematically illustrating a dual turbo centrifugal chiller 201 according to another embodiment.
  • As illustrated in FIG. 3, in the dual turbo centrifugal chiller 201 according to this embodiment, a first evaporator 221 and a second evaporator 222 are connected in parallel. Cold water 223 flows into an end of the first evaporator 221 connected in parallel and flows out of the other end of the first evaporator 221, flows into an end of the second evaporator 222, passes through the second evaporator 222, and flows out of the other end of the second evaporator 222.
  • A first condenser 211 and a second condenser 212 are connected in parallel. Cooling water 213 flows into an end of the first condenser 211 connected in parallel, flows out of the other end of the first condenser 211, flows into an end of the second condenser 212, passes through the second condenser 212, and flows out of the other end of the second condenser 212.
  • A first compressor 231 is connected to the first condenser 211 and the second evaporator 222, and a refrigerant of the first compressor 231 is circulated to exchange heat with the cooling water of the first condenser 211 and the cold water of the second evaporator 222. A second compressor 232 is connected to the second condenser 212 and the first evaporator 221, and a refrigerant of the second compressor 232 is circulated to exchange heat with the cooling water of the second condenser 212 and the cold water of the first evaporator 221.
  • Here, a temperature of the cold water that flows into the first evaporator 221 is 12° C., a temperature of the cold water that flows out of the second evaporator 222 is 7° C., a temperature of the cooling water that flows into the first condenser 211 is 32° C., and a temperature of the cooling water that flows out of the second condenser 212 is 37° C.
  • Without consideration of LTDs of the evaporators and the compressors, a head of the first compressor 231 is 27.5° C. (34.5° C.-7° C.), and a head of the second compressor 232 is also 27.5° C. (37° C.-9.5° C.). That is, the heads of the two compressors are equal to each other.
  • Since connection relationships between impellers 245, 246, 247, and 248 of the compressors 231 and 232, the rotation shaft 161, a gear 262, and a driving unit 263 provided in the dual turbo centrifugal chiller 201 according to this embodiment, and a flow of a refrigerant 251, 252, 253, and 254 at inlet and outlet portions 243 and 244 of the compressor are the same as those of the embodiment illustrated in FIG. 2, a detailed description thereof will be omitted.
  • Although the two embodiments of the dual turbo centrifugal chiller have been described, this disclosure is not limited thereto. That is to say, the two evaporators may be connected in serial or in parallel, and the two condensers may be connected in serial or in parallel. In this case, it should be understood by those skilled in the art that cold water passes through a first evaporator and a second evaporator, cooling water passes through a second condenser after passing through a first condenser, a first compressor containing a refrigerant is connected to the first condenser and the second evaporator, and a second compressor containing a refrigerant is connected to the second condenser and the first evaporator, thereby implementing a dual turbo centrifugal chiller in which heads of the two compressor are equal to each other.
  • While the exemplary embodiments have been shown and described, it will be understood by those skilled in the art that various changes in form and details may be made thereto without departing from the spirit and scope of this disclosure as defined by the appended claims.
  • In addition, many modifications can be made to adapt a particular situation or material to the teachings of this disclosure without departing from the essential scope thereof. Therefore, it is intended that this disclosure not be limited to the particular exemplary embodiments disclosed as the best mode contemplated for carrying out this disclosure, but that this disclosure will include all embodiments falling within the scope of the appended claims.

Claims (5)

1. A dual turbo centrifugal chiller, comprising:
first and second evaporators connected in series or in parallel;
first and second condensers connected in series or in parallel; and
first and second compressors including impellers,
wherein cold water passes through the second evaporator after passing through the first evaporator, and cooling water passes through the second condenser after passing through the first condenser,
the first compressor containing a refrigerant connects the first condenser to the second evaporator, and the second compressor containing a refrigerant connects the second condenser to the first evaporator, and
the impellers of the first compressor and second compressor are rotated simultaneously using a single driving unit.
2. The dual turbo centrifugal chiller according to claim 1,
wherein the impellers of the first and second compressors are connected with a single rotation shaft, and
the impellers of the first and second compressor are rotated simultaneously as the rotation shaft is rotated using the driving unit.
3. The dual turbo centrifugal chiller according to claim 2,
wherein the driving unit is connected to the center of the rotation shaft, and
the impellers of the first and second compressors are opposed with the center of the rotation shaft between them.
4. The dual turbo centrifugal chiller according to claim 1, wherein inlet portions of the first and second compressors are provided with inlet guide vanes (IGVs) respectively.
5. The dual turbo centrifugal chiller according to claim 3, wherein the first and second compressors have different capacities from each other.
US12/796,014 2009-10-27 2010-06-08 Dual turbo centrifugal chiller Abandoned US20110094251A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
KR10-2009-0102209 2009-10-27
KR1020090102209A KR101065549B1 (en) 2009-10-27 2009-10-27 Dual Turbo Centrifugal Chiller

Publications (1)

Publication Number Publication Date
US20110094251A1 true US20110094251A1 (en) 2011-04-28

Family

ID=43897216

Family Applications (1)

Application Number Title Priority Date Filing Date
US12/796,014 Abandoned US20110094251A1 (en) 2009-10-27 2010-06-08 Dual turbo centrifugal chiller

Country Status (3)

Country Link
US (1) US20110094251A1 (en)
KR (1) KR101065549B1 (en)
CN (1) CN102052796A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103615842A (en) * 2013-10-29 2014-03-05 广州市盈夏制冷技术有限公司 Overall energy-saving compressor device
WO2015089362A1 (en) * 2013-12-12 2015-06-18 Johnson Controls Technology Company Steam turbine driven centrifugal heat pump
US20230296243A1 (en) * 2021-06-16 2023-09-21 Colorado State University Research Foundation Air source heat pump system and method of use for industrial steam generation

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101372353B1 (en) * 2011-12-21 2014-03-13 정방균 Heat pump system using a turbo compressor
KR102201745B1 (en) * 2014-05-20 2021-01-12 엘지전자 주식회사 Turbo chiller and chiller system comprising the same
CN104235988B (en) * 2014-10-16 2017-02-01 珠海格力电器股份有限公司 Centrifugal air conditioning unit using water as refrigerant and operation method
EP3931503A1 (en) 2019-02-27 2022-01-05 Johnson Controls Tyco IP Holdings LLP Condenser arrangement for a chiller

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5845509A (en) * 1997-09-26 1998-12-08 Shaw; David N. Variable speed parallel centrifugal compressors for HVAC and refrigeration systems
US5875637A (en) * 1997-07-25 1999-03-02 York International Corporation Method and apparatus for applying dual centrifugal compressors to a refrigeration chiller unit
US5996356A (en) * 1996-10-24 1999-12-07 Mitsubishi Heavy Industries, Ltd. Parallel type refrigerator
US20030233838A1 (en) * 2002-06-19 2003-12-25 Lg Electronics Inc. Air conditioning system with two compressors and method for operating the same
US6772599B2 (en) * 2002-08-06 2004-08-10 York International Corporation Stability control system and method for compressors operating in parallel
US7240515B2 (en) * 2002-02-28 2007-07-10 Turbocor, Inc. Centrifugal compressor
WO2008045039A1 (en) * 2006-10-10 2008-04-17 Carrier Corporation Dual-circuit chiller with two-pass heat exchanger in a series counterflow arrangement

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SE419128B (en) 1974-09-05 1981-07-13 Projectus Ind Produkter Ab PROCEDURE FOR OPERATION OF HEAT PUMP INSTALLATION
JPS5926206Y2 (en) 1979-12-22 1984-07-30 ダイキン工業株式会社 Heat recovery centrifugal refrigerator
JPH07120084A (en) * 1993-10-27 1995-05-12 Ebara Corp Turbo-refrigerator
JPH10131889A (en) * 1996-10-25 1998-05-19 Mitsubishi Heavy Ind Ltd Compressor for perforator
KR100378531B1 (en) 2001-04-11 2003-04-03 엘지전선 주식회사 coolant and oil separating/ collecting device of turbo chiller
CN1405457A (en) * 2001-09-20 2003-03-26 成都希望电子研究所 Centrifugal refrigeration compressing apparatus
JP2007177695A (en) * 2005-12-28 2007-07-12 Ishikawajima Harima Heavy Ind Co Ltd Turbo compressor

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5996356A (en) * 1996-10-24 1999-12-07 Mitsubishi Heavy Industries, Ltd. Parallel type refrigerator
US5875637A (en) * 1997-07-25 1999-03-02 York International Corporation Method and apparatus for applying dual centrifugal compressors to a refrigeration chiller unit
US5845509A (en) * 1997-09-26 1998-12-08 Shaw; David N. Variable speed parallel centrifugal compressors for HVAC and refrigeration systems
US7240515B2 (en) * 2002-02-28 2007-07-10 Turbocor, Inc. Centrifugal compressor
US20030233838A1 (en) * 2002-06-19 2003-12-25 Lg Electronics Inc. Air conditioning system with two compressors and method for operating the same
US6772599B2 (en) * 2002-08-06 2004-08-10 York International Corporation Stability control system and method for compressors operating in parallel
WO2008045039A1 (en) * 2006-10-10 2008-04-17 Carrier Corporation Dual-circuit chiller with two-pass heat exchanger in a series counterflow arrangement

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103615842A (en) * 2013-10-29 2014-03-05 广州市盈夏制冷技术有限公司 Overall energy-saving compressor device
WO2015089362A1 (en) * 2013-12-12 2015-06-18 Johnson Controls Technology Company Steam turbine driven centrifugal heat pump
US10704810B2 (en) 2013-12-12 2020-07-07 Johnson Controls Technology Company Steam turbine driven centrifugal heat pump
US20230296243A1 (en) * 2021-06-16 2023-09-21 Colorado State University Research Foundation Air source heat pump system and method of use for industrial steam generation

Also Published As

Publication number Publication date
KR20110045574A (en) 2011-05-04
KR101065549B1 (en) 2011-09-19
CN102052796A (en) 2011-05-11

Similar Documents

Publication Publication Date Title
US20110094251A1 (en) Dual turbo centrifugal chiller
US10215444B2 (en) Heat exchanger having stacked coil sections
US6698234B2 (en) Method for increasing efficiency of a vapor compression system by evaporator heating
EP2223021B1 (en) Refrigerating system and method for refrigerating
WO2014013670A1 (en) Heat management system for vehicle
US20020050149A1 (en) Multistage compression refrigerating machine for supplying refrigerant from intercooler to cool rotating machine and lubricating oil
EP1803593B1 (en) Air conditioning systems for vehicles
US11578901B2 (en) Cooling fan for refrigerant cooled motor
EP2165135B1 (en) Refrigerating system
US20040031286A1 (en) Suction connection for dual centrifugal compressor refrigeration systems
EP2693138B1 (en) Centrifugal chiller
WO2024020019A1 (en) Compressor system for heating, ventilation, air conditioning & refrigeration system
US9109816B2 (en) Mechanical subcooling of transcritical R-744 refrigeration systems with heat pump heat reclaim and floating head pressure
KR101658223B1 (en) Cooling-Storage System
US20110171015A1 (en) Centrifugal compressor and fabricating method thereof
US20220170467A1 (en) Multi-pump apparatus of cooling system
WO2012037021A2 (en) Compressor having an oil management system
CN101435629B (en) Screw type cold source hot water machine unit
CN114211933B (en) Low-temperature heat pump air conditioning system and working method thereof
CN216672796U (en) Motor cooling system of refrigeration centrifugal compressor
US20230137972A1 (en) Centrifugal compressor with reverse overhung volute
US11015848B2 (en) Axial flow compressor for HVAC chiller systems
WO2023244819A1 (en) Compressor system for hvac&r system
CN115200268A (en) Heat exchange circulation system, air conditioner and vehicle
JP2004037010A (en) Heat exchanger

Legal Events

Date Code Title Description
AS Assignment

Owner name: LS MTRON LTD., KOREA, REPUBLIC OF

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:KIM, KIL YOUNG;KIM, JIN SUNG;KANG, TAE JIN;REEL/FRAME:024501/0382

Effective date: 20100427

AS Assignment

Owner name: LG ELECTRONICS INC., KOREA, REPUBLIC OF

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:LS MTRON, LTD.;REEL/FRAME:026332/0394

Effective date: 20110512

STCB Information on status: application discontinuation

Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION