CN202041016U - Centrifugal unit - Google Patents

Centrifugal unit Download PDF

Info

Publication number
CN202041016U
CN202041016U CN201120091640XU CN201120091640U CN202041016U CN 202041016 U CN202041016 U CN 202041016U CN 201120091640X U CN201120091640X U CN 201120091640XU CN 201120091640 U CN201120091640 U CN 201120091640U CN 202041016 U CN202041016 U CN 202041016U
Authority
CN
China
Prior art keywords
condenser
compressor
low pressure
pressure compressor
valve body
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.)
Expired - Lifetime
Application number
CN201120091640XU
Other languages
Chinese (zh)
Inventor
张明研
刘华
李宏波
张治平
姜国璠
王晨光
王彦川
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.)
Gree Electric Appliances Inc of Zhuhai
Original Assignee
Gree Electric Appliances Inc of Zhuhai
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 Gree Electric Appliances Inc of Zhuhai filed Critical Gree Electric Appliances Inc of Zhuhai
Priority to CN201120091640XU priority Critical patent/CN202041016U/en
Application granted granted Critical
Publication of CN202041016U publication Critical patent/CN202041016U/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Landscapes

  • Structures Of Non-Positive Displacement Pumps (AREA)

Abstract

The utility model provides a centrifugal unit, which comprises an evaporator, a low pressure compressor and a condenser which are mutually connected, and also comprises a high pressure compressor connected in series with the low pressure compressor in a twin-stage manner, and an economizer connected between the condenser and the evaporator, wherein a first valve body K1 is arranged between the low pressure compressor and the condenser; a second valve body K2 is connected and arranged between the low pressure compressor and the economizer; and a third valve body K3 is arranged between the high pressure compressor and the condenser. Further, a throttling device is arranged between the condenser and the evaporator; a high pressure throttling valve is arranged between the condenser and the economizer; and a low pressure throttling valve is arranged between the economizer and the evaporator. The centrifugal unit provided by the utility model can simultaneously perform the functions of refrigeration, heating and ice thermal storage, so the usable range of the centrifugal cold water unit is expanded.

Description

A kind of centrifugal unit
[technical field]
The utility model relates to field of air conditioning, refers in particular to a kind of centrifugal unit.
[background technology]
Along with economic development, the domestic city scale progressively increases, and the original heating system in city can't satisfy existing demand, and it is high and pollute few advantage to utilize heat pump heat supply to have efficient, is progressively accepted by people.Central heating is taked in city, the north more, and centrifugal unit refrigeration and the big advantage of heating capacity can better be brought into play.Centrifugal unit is owing to have big cold, high performance advantage, be widely used in large scale business, industrial site, but himself characteristic decision centrifugal compressor can only bear less pressure ratio, can only realize single cold pattern, exist and to realize the shortcoming that heats and ice cool storage function can not satisfying existing demand.And, what most of centrifugal units adopted all is that two conventional compressors are connected, because self there is an optimum pressure ratio operating point in conventional centrifugal compressor, if two of series connection all is conventional compressor, depart from the optimum pressure ratio operating point when then causing compressor operating easily, the compressor adiabatic efficiency is obviously descended.
[summary of the invention]
The purpose of this utility model is to provide a kind of and can realizes simultaneously freezing, the centrifugal unit of heat-production functions.
For realizing the utility model purpose, provide following technical scheme:
The utility model provides a kind of centrifugal unit, it comprises evaporimeter, low pressure compressor and the condenser that is connected, be provided with throttling arrangement between this condenser and the evaporimeter, it also comprises the high pressure compressor of realizing double stage tandem with low pressure compressor, and be connected economizer between condenser and the evaporimeter, be provided with the first valve body K1 between this low pressure compressor and the condenser, be connected between this low pressure compressor and the economizer and be provided with the second valve body K2, be provided with the 3rd valve body K3 between this high pressure compressor and the condenser.
The present invention is a kind of centrifugal unit of high pressure ratio of two-shipper head series connection, can realize refrigeration simultaneously, heats or ice cool storage function.During separate refrigeration, only allow the low pressure compressor operation; Heat or when icing cold-storage low pressure compressor and high pressure compressor series operation.
Preferably, the described first valve body K1, the second valve body K2 and the 3rd valve body K3 are stop valve.This stop valve is realized the break-make of pipeline easily, and control is got up rapider, more convenient and more effective.
Preferably, be provided with the high pressure choke valve between described condenser and the economizer, be provided with the low pressure choke valve between economizer and the evaporimeter.Make system more perfect, can the refrigerant in the system be control effectively.
Preferably, this low pressure compressor generally adopts conventional refrigeration compressor, high pressure compressor redesigns according to high pressure ratio real work operating mode, the pressure ratio scope that adopts pressure at expulsion and pressure of inspiration(Pi) is 1.2 to 2.6 little pressure ratio compressor, can guarantee that two compressors all can realize higher adiabatic efficiency.
The concrete operation principle of the centrifugal unit of the utility model is as follows:
During refrigeration mode, K2, K3 close, and K1 opens, and high pressure choke valve and low pressure choke valve are stopped using, and refrigerant enters the low pressure compressor compression through evaporimeter, enters condenser condenses, enters evaporator evaporation after the choke valve throttling, finishes kind of refrigeration cycle.
When heating/icing the cold-storage pattern, K2, K3 open, K1 closes, and throttling arrangement is stopped using, and refrigerant is after evaporimeter enters the low pressure compressor compression, enter the high pressure compressor compression once more, enter condenser condenses then, enter the economizer shwoot through the high pressure choke valve after the condensation, gaseous coolant becomes the high pressure compressed tonifying Qi behind the shwoot, other liquid refrigerants enter evaporation through the low pressure choke valve, finish whole circulation.
The contrast prior art the utlity model has following advantage:
The centrifugal unit of the utility model can realize freezing, heating, ice cool storage function simultaneously, expands the centrifugal water chillers scope of application; In addition, low pressure compressor adopts different pressure ratios with high pressure compressor, thus when guaranteeing the single-stage refrigeration and twin-stage heat/when icing cold-storage higher adiabatic efficiency can be arranged.
[description of drawings]
Fig. 1 is the structural representation of the centrifugal unit of the utility model.
[specific embodiment]
See also Fig. 1, the utility model is a kind of centrifugal unit of high pressure ratio of two-shipper head series connection, it comprises the evaporimeter 1 that is connected, low pressure compressor 2, condenser 3, be provided with throttling arrangement 13 between condenser 3 and the evaporimeter 1, also comprise the high pressure compressor 4 of realizing double stage tandem with low pressure compressor 2, and be connected economizer 5 between condenser 3 and the evaporimeter 1, be provided with the first valve body K1 between this low pressure compressor 2 and the condenser 3, be connected between this low pressure compressor 2 and the economizer 5 and be provided with the second valve body K2, be provided with the 3rd valve body K3 between this high pressure compressor 4 and the condenser 3, be provided with high pressure choke valve 35 between this condenser 3 and the economizer 5, be provided with low pressure choke valve 15 between this economizer 5 and the evaporimeter 1.Described throttling arrangement 13 can be selected choke valve or capillary throttle pipe etc.The described first valve body K1, the second valve body K2 and the 3rd valve body K3 are stop valve.Described high pressure compressor adopts little pressure ratio compressor, and the pressure ratio scope of the pressure at expulsion of this little pressure ratio compressor and pressure of inspiration(Pi) is 1.2 to 2.6.
Centrifugal compressor can only be realized refrigeration mode at present, can reach pressure ratio and have only 2.6-2.7, generally needs more than 4.0 and heat or ice cold-storage operating mode pressure ratio, therefore needs double-compressor series connection compression.Because what most of centrifugal units adopted all is that two conventional compressors are connected, because self there is an optimum pressure ratio operating point in conventional centrifugal compressor, if two of series connection all is conventional compressor, depart from the optimum pressure ratio operating point when then causing compressor operating easily, the compressor adiabatic efficiency is obviously descended.So in the present embodiment, this high pressure compressor adopts little pressure ratio centrifugal compressor, calculation Design impeller according to the actual requirements, thus guarantee that under the series operation operating mode, two compressors all guarantee higher adiabatic efficiency.
During refrigeration mode, K2, K3 close, and K1 opens, and high pressure choke valve and low pressure choke valve are stopped using, and refrigerant enters the low pressure compressor compression through evaporimeter, enters condenser condenses, enters evaporator evaporation after the throttling arrangement throttling, finishes kind of refrigeration cycle; Heat/ice the cold-storage pattern, K2, K3 open, K1 closes, and choke valve is stopped using, and refrigerant is after evaporimeter enters the low pressure compressor compression, enter the high pressure compressor compression once more, enter condenser condenses then, enter the economizer shwoot through the high pressure choke valve after the condensation, gaseous coolant becomes the high pressure compressed tonifying Qi behind the shwoot, other liquid refrigerants enter evaporation through the low pressure choke valve, finish whole circulation.
The above only is preferred embodiment of the present utility model, and protection domain of the present utility model is not limited thereto, and anyly all belongs within the utility model protection domain based on the equivalent transformation on the technical solutions of the utility model.

Claims (5)

1. centrifugal unit, it comprises evaporimeter, low pressure compressor and the condenser that is connected, be provided with throttling arrangement between this condenser and the evaporimeter, it is characterized in that, it also comprises the high pressure compressor of realizing double stage tandem with low pressure compressor, and be connected economizer between condenser and the evaporimeter, be provided with the first valve body K1 between this low pressure compressor and the condenser, be connected between this low pressure compressor and the economizer and be provided with the second valve body K2, be provided with the 3rd valve body K3 between this high pressure compressor and the condenser.
2. centrifugal unit as claimed in claim 1 is characterized in that, the described first valve body K1, the second valve body K2 and the 3rd valve body K3 are stop valve.
3. centrifugal unit as claimed in claim 1 is characterized in that, is provided with the high pressure choke valve between described condenser and the economizer, is provided with the low pressure choke valve between economizer and the evaporimeter.
4. as any described centrifugal unit of claim 1 to 3, it is characterized in that described high pressure compressor adopts little pressure ratio compressor.
5. centrifugal unit as claimed in claim 4 is characterized in that, the pressure ratio scope of the pressure at expulsion of described little pressure ratio compressor and pressure of inspiration(Pi) is 1.2 to 2.6.
CN201120091640XU 2011-03-31 2011-03-31 Centrifugal unit Expired - Lifetime CN202041016U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201120091640XU CN202041016U (en) 2011-03-31 2011-03-31 Centrifugal unit

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201120091640XU CN202041016U (en) 2011-03-31 2011-03-31 Centrifugal unit

Publications (1)

Publication Number Publication Date
CN202041016U true CN202041016U (en) 2011-11-16

Family

ID=44968457

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201120091640XU Expired - Lifetime CN202041016U (en) 2011-03-31 2011-03-31 Centrifugal unit

Country Status (1)

Country Link
CN (1) CN202041016U (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103335441A (en) * 2013-07-04 2013-10-02 天津商业大学 Secondary throttling middle incomplete cooling variable flow double-stage compression refrigeration system
CN103335440A (en) * 2013-07-04 2013-10-02 天津商业大学 Secondary throttling middle complete cooling double-working-condition refrigeration system
CN104344610A (en) * 2013-08-01 2015-02-11 珠海格力电器股份有限公司 Air conditioning unit
CN111059657A (en) * 2019-12-11 2020-04-24 珠海格力电器股份有限公司 Refrigeration and ice-making air conditioning unit and control method

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103335441A (en) * 2013-07-04 2013-10-02 天津商业大学 Secondary throttling middle incomplete cooling variable flow double-stage compression refrigeration system
CN103335440A (en) * 2013-07-04 2013-10-02 天津商业大学 Secondary throttling middle complete cooling double-working-condition refrigeration system
CN104344610A (en) * 2013-08-01 2015-02-11 珠海格力电器股份有限公司 Air conditioning unit
CN104344610B (en) * 2013-08-01 2016-08-24 珠海格力电器股份有限公司 Air-conditioner set
CN111059657A (en) * 2019-12-11 2020-04-24 珠海格力电器股份有限公司 Refrigeration and ice-making air conditioning unit and control method

Similar Documents

Publication Publication Date Title
CN103776189B (en) Tonifying Qi for the band injector of heat pump assembly increases enthalpy type heat pump circulating system
CN201344676Y (en) Heat pump air conditioner with by-pass super-cooling
CN102032705B (en) Two-stage compression heat pump system
CN104110908A (en) Three-stage compression cascade circulation heat pump system and control method thereof
CN202002391U (en) Water heater unit with spray liquid enthalpy-increasing heat pump
CN202254464U (en) Trans-critical carbon dioxide (CO2) circulating refrigeration system
CN107763892B (en) Defrosting air source heat pump system
CN202420015U (en) Air-conditioning and refrigeration integrated unit for outdoor type convenience store
CN102022793A (en) Latent heat recovery-based high-efficiency heat pump type heat source tower solution regenerating device and method
CN103398485A (en) Steam compression refrigerating system device and supercooling method
CN103615836A (en) Screw type total heat recovery air cooled heat pump air conditioning unit
CN1854645A (en) Geothermal heat-pumping system
CN202041016U (en) Centrifugal unit
CN201053785Y (en) Heat pump air conditioner
CN203605512U (en) Air-cooling type compression condensing unit with supercooled gas-liquid separator
CN106705494A (en) Air source heat pump energy conservation system with function of preventing air side heat exchanger from freezing
CN201875830U (en) Latent heat recycling based efficient heat pump-type device for regenerating solutions in heat-source tower
CN204063660U (en) Three stage compression autocascade cycle heat pump
CN103836792A (en) Heat pump and hot water heating combination system
CN104359177B (en) Total heat recovery formula multifunctional cold and hot water unit
CN203464542U (en) Air source low-temperature two-stage compression heat pump air conditioner
CN203203288U (en) Air conditioner
CN112524832A (en) Novel air-conditioning refrigeration system adopting carbon dioxide for refrigeration
CN205227902U (en) Carbon dioxide secondary refrigerant refrigerating unit
CN101487643A (en) Ultra-low temperature heat pump air conditioning system

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CX01 Expiry of patent term

Granted publication date: 20111116

CX01 Expiry of patent term