CN105674634A - Freon hydraulic filling type system flashing barrel economizer - Google Patents
Freon hydraulic filling type system flashing barrel economizer Download PDFInfo
- Publication number
- CN105674634A CN105674634A CN201610030236.9A CN201610030236A CN105674634A CN 105674634 A CN105674634 A CN 105674634A CN 201610030236 A CN201610030236 A CN 201610030236A CN 105674634 A CN105674634 A CN 105674634A
- Authority
- CN
- China
- Prior art keywords
- compressor
- flash distillation
- liquid
- bucket
- barrel
- 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.)
- Granted
Links
Classifications
-
- 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
- F25B41/00—Fluid-circulation arrangements
- F25B41/40—Fluid line arrangements
-
- 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
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
The invention belongs to the technical field of refrigeration, and relates to a Freon hydraulic filling type system flashing barrel economizer. The Freon hydraulic filling type system flashing barrel economizer comprises a flashing barrel, a primary throttling valve, a liquid supply electromagnetic valve, a gas supplementing electromagnetic valve, a one-way valve and a secondary throttling valve. The flashing barrel is connected with a high-pressure liquid storage device through the primary throttling valve and the liquid supply electromagnetic valve. The flashing barrel is connected with a low-pressure circulation barrel through the secondary throttling valve. The flashing barrel is connected with a compressor through the gas supplementing electromagnetic valve and the one-way valve. The high-pressure liquid storage device is connected with a condenser, and the condenser is connected with the compressor. The compressor is connected with the low-pressure circulation barrel. An inlet of the low-pressure circulation barrel is connected with an evaporator. An outlet of the low-pressure circulation barrel is connected with the evaporator through the one-way valve. According to the Freon hydraulic filling type system flashing barrel economizer, the refrigerating capacity and the energy efficiency ratio of the system can be improved, it can be guaranteed that liquid does not return in a medium-pressure gas supplementing port of the compressor, and running of the compressor is safer.
Description
Technical field
The invention belongs to refrigeration technology field, be specifically related to freon full-liquid type system flash distillation bucket economizer device.
Background technology
Under high pressure ratio cooling condition, the screw compression with intermediate pressure gas supplementing opening condenses unit, or twin-stage joins dozen compressor bank, generally will run by band charge air cooler. The refrigerating capacity of unit can be improved on the one hand; The deficient compressive state of compressor can be improved on the other hand, improve the COP value of compressor. We are called economizer (ECO) this charge air cooler.
In freon system, most domestic unit manufacturer all adopts plate type heat exchanger to do economizer. This is a kind of economizer cycle once throttled, and economizer has 8-10K heat transfer temperature difference. Its shortcoming is to have heat transfer temperature loss, and economizer expansion valve is often because load variations causes compressor to return liquid beyond its range of accommodation greatly, increases the risk of compressor abrasion, causes that compressor is short for service life.
Summary of the invention
The invention aims to improve the service life of compressor, improve the Energy Efficiency Ratio of refrigeration system.
Technical scheme: freon full-liquid type system flash distillation bucket economizer device, is characterized in that including flash distillation bucket, choke valve, liquid supply electromagnetic valve, QI invigorating electromagnetic valve, check valve, a second throttle valve; Flash distillation bucket is connected with high-pressure reservoir by a choke valve and liquid supply electromagnetic valve, and flash distillation bucket is connected with low pressure recycle bucket by second throttle valve; Flash distillation bucket is connected with compressor by QI invigorating electromagnetic valve and check valve, and high-pressure reservoir is connected with condenser, and condenser is connected with compressor; Compressor connects low pressure recycle bucket, and the import of low pressure recycle bucket connects vaporizer, and the outlet of low pressure recycle bucket connects vaporizer by check valve.
Arranging liquid level controller in described flash distillation bucket, liquid level controller connects liquid supply electromagnetic valve.
The operation principle of freon full-liquid type system flash distillation bucket economizer device: condensed refrigerant liquid enters high-pressure reservoir, and to become pressure be that 11 ~ 18bar(depends on cold-producing medium and condensation temperature) high-pressure refrigerant, the first time throttling entrance flash distillation bucket that passes through of high-pressure refrigerant becomes middle compression refrigerant, the force value of middle compression refrigerant (1.3~5.8bar identical with the force value at the middle pressure gas supplementing opening place of compressor, depend on cold-producing medium and evaporating temperature), cold-producing medium gasifies a part of (the more low ratio of 20%~38% evaporating temperature is more big) in the process of blood pressure lowering, remaining refrigerant liquid obtains cooling, the gas of flash distillation bucket shwoot is therefrom pressed gas supplementing opening to siphon away by compressor,Remaining refrigerant liquid is not because have heat transfer temperature loss, and its degree of supercooling becomes more greatly supercool saturated liquid (be supercool relative to condensation temperature, but because throttle and be saturated liquid), and supercool saturated liquid enters low pressure recycle bucket through second throttle.
The economizer device of the present invention can obtain bigger degree of supercooling thus improve the Energy Efficiency Ratio of refrigeration system, can prevent compressor from returning the risk of liquid simultaneously.
Flash distillation bucket of the present invention does not have heat transfer temperature loss, and Energy Efficiency Ratio is higher.
Have compared with the economizer of 8-10K heat transfer temperature difference with plate type heat exchanger, the present invention can obtain the liquid of more big supercooling degree and improve 5-6% to vaporizer feed flow, refrigerating capacity and Energy Efficiency Ratio.
Flash distillation bucket of the present invention, with liquid level controller, can guarantee that and presses gas supplementing opening not return liquid in compressor, and compressor operating is safer.
Accompanying drawing explanation
Fig. 1 is the structural representation of the present invention.
In figure, 1, flash distillation bucket, 2, choke valve, 3, liquid supply electromagnetic valve, 4, liquid level controller, 5, QI invigorating electromagnetic valve, 6, check valve, 7, second throttle valve, 8, compressor, 9, condenser, 10, high-pressure reservoir, 11, low pressure recycle bucket.
Detailed description of the invention
Freon full-liquid type system flash distillation bucket economizer device, is characterized in that being made up of flash distillation bucket, choke valve, liquid supply electromagnetic valve, liquid level controller, QI invigorating electromagnetic valve, check valve, a second throttle valve; Flash distillation bucket is connected with high-pressure reservoir by a choke valve and liquid supply electromagnetic valve, and flash distillation bucket is connected with low pressure recycle bucket by second throttle valve; Flash distillation bucket is connected with compressor by QI invigorating electromagnetic valve and check valve, and high-pressure reservoir is connected with condenser, and condenser is connected with compressor; Compressor connects low pressure recycle bucket, and the import of low pressure recycle bucket connects vaporizer, and the outlet of low pressure recycle bucket connects vaporizer by check valve. Arranging liquid level controller in described flash distillation bucket, liquid level controller connects liquid supply electromagnetic valve.
Condensed refrigerant liquid enters high-pressure reservoir, and to become pressure be that 11 ~ 18bar(depends on cold-producing medium and condensation temperature) high-pressure refrigerant, the first time throttling entrance flash distillation bucket that passes through of high-pressure refrigerant becomes middle compression refrigerant, the force value of middle compression refrigerant (1.3~5.8bar identical with the force value at the middle pressure gas supplementing opening place of compressor, depend on cold-producing medium and evaporating temperature), cold-producing medium gasifies in the process of blood pressure loweringA part(the more low ratio of 20%~38% evaporating temperature is more big), remaining refrigerant liquid obtains cooling, and the gas of flash distillation bucket shwoot cools remaining refrigerant liquid in bucket therefrom being pressed gas supplementing opening by compressor while siphoning away; Remaining refrigerant liquid is not because having heat transfer temperature loss, and its degree of supercooling becomes more greatly supercool saturated liquid, and supercool saturated liquid enters low pressure recycle bucket through second throttle.
Liquid level in flash distillation bucket is controlled liquid supply electromagnetic valve 3 by liquid level controller 4, it is ensured that liquid level can not be too high. QI invigorating electromagnetic valve 5 machine by compression controls, and compressor is opened and reached economizer device and puts into condition, and QI invigorating electromagnetic valve 5 is opened, and during compressor shutdown, QI invigorating electromagnetic valve 5 cuts out.
Claims (3)
1. freon full-liquid type system flash distillation bucket economizer device, is characterized in that including flash distillation bucket, choke valve, liquid supply electromagnetic valve, QI invigorating electromagnetic valve, check valve, a second throttle valve; Flash distillation bucket is connected with high-pressure reservoir by a choke valve and liquid supply electromagnetic valve, and flash distillation bucket is connected with low pressure recycle bucket by second throttle valve; Flash distillation bucket is connected with compressor by QI invigorating electromagnetic valve and check valve, and high-pressure reservoir is connected with condenser, and condenser is connected with compressor; Compressor connects low pressure recycle bucket, and the import of low pressure recycle bucket connects vaporizer, and the outlet of low pressure recycle bucket connects vaporizer by check valve.
2. freon full-liquid type system flash distillation bucket economizer device according to claim 1,
It is characterized in that arranging liquid level controller in described flash distillation bucket, liquid level controller connects liquid supply electromagnetic valve.
3. freon full-liquid type system flash distillation bucket economizer device according to claim 1,
It is characterized in that condensed refrigerant liquid enters high-pressure reservoir and becomes the high-pressure refrigerant that pressure is 11 ~ 18bar, the first time throttling entrance flash distillation bucket that passes through of high-pressure refrigerant becomes middle compression refrigerant, the force value of middle compression refrigerant 1.3~5.8bar identical with the force value at the middle pressure gas supplementing opening place of compressor, cold-producing medium gasifies 20%~38% in the process of blood pressure lowering, remaining refrigerant liquid obtains cooling, and the gas of flash distillation bucket shwoot is therefrom pressed gas supplementing opening to siphon away by compressor; Remaining refrigerant liquid is not because having heat transfer temperature loss, and its degree of supercooling becomes more greatly supercool saturated liquid, and supercool saturated liquid enters low pressure recycle bucket through second throttle.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201610030236.9A CN105674634B (en) | 2016-01-18 | 2016-01-18 | Freon full-liquid type system flashes bucket economizer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201610030236.9A CN105674634B (en) | 2016-01-18 | 2016-01-18 | Freon full-liquid type system flashes bucket economizer |
Publications (2)
Publication Number | Publication Date |
---|---|
CN105674634A true CN105674634A (en) | 2016-06-15 |
CN105674634B CN105674634B (en) | 2017-12-29 |
Family
ID=56301248
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201610030236.9A Active CN105674634B (en) | 2016-01-18 | 2016-01-18 | Freon full-liquid type system flashes bucket economizer |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN105674634B (en) |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106705505A (en) * | 2017-02-27 | 2017-05-24 | 莱芜市图腾制冷设备有限公司 | Efficient combined type flash drum pump unit |
CN106969556A (en) * | 2016-12-31 | 2017-07-21 | 广州市粤联水产制冷工程有限公司 | A kind of flash type economizer and cooling cycle system |
CN106969516A (en) * | 2016-12-31 | 2017-07-21 | 广州市粤联水产制冷工程有限公司 | A kind of refrigerating method and cooling cycle system |
CN107677001A (en) * | 2017-09-15 | 2018-02-09 | 北京市京科伦冷冻设备有限公司 | A kind of independent humidification-type fruits and vegetables ice temperature stereo garage carbon dioxide refrigerating system |
CN108072190A (en) * | 2017-12-26 | 2018-05-25 | 珠海格力电器股份有限公司 | Air-conditioning system and with its air conditioner |
CN110044132A (en) * | 2019-05-15 | 2019-07-23 | 南京福加自动化科技有限公司 | A kind of propylene full-liquid type refrigeration system and control method |
CN110631281A (en) * | 2019-10-21 | 2019-12-31 | 无锡职业技术学院 | Natural cooling refrigerating system |
CN112368528A (en) * | 2019-06-07 | 2021-02-12 | 开利公司 | Modular water side economizer integrated with air cooling chiller |
Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4231229A (en) * | 1979-03-21 | 1980-11-04 | Emhart Industries, Inc. | Energy conservation system having improved means for controlling receiver pressure |
CN201062900Y (en) * | 2007-07-30 | 2008-05-21 | 无锡同方人工环境有限公司 | Low temperature air-cooling hot pump system |
CN201885478U (en) * | 2010-12-20 | 2011-06-29 | 天津柯瑞斯空调设备有限公司 | Low temperature type air source heat pump unit |
CN202734344U (en) * | 2012-07-05 | 2013-02-13 | 泰豪科技股份有限公司 | Low temperature enthalpy increasing family type central air conditioner |
CN103471275A (en) * | 2013-08-30 | 2013-12-25 | 青岛海信日立空调系统有限公司 | Enhanced vapor injection air-conditioning circulating system and control method thereof |
CN203443292U (en) * | 2013-07-18 | 2014-02-19 | 成都蓉阳科技有限公司 | Integrated heat-pump drying unit for dehumidification, low-temperature air spraying and enthalpy increase of fresh air of air source |
CN203586601U (en) * | 2013-09-27 | 2014-05-07 | 深圳麦克维尔空调有限公司 | Enhanced-vapour-injection type air-conditioning device |
CN103851828A (en) * | 2014-03-28 | 2014-06-11 | 佛山市顺德区华天成电器有限公司 | Enhanced vapor injection combined system |
CN205316749U (en) * | 2016-01-18 | 2016-06-15 | 山西永有制冷科技有限公司 | Economic ware of freon hydraulic filling formula system's flash distillation bucket |
-
2016
- 2016-01-18 CN CN201610030236.9A patent/CN105674634B/en active Active
Patent Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4231229A (en) * | 1979-03-21 | 1980-11-04 | Emhart Industries, Inc. | Energy conservation system having improved means for controlling receiver pressure |
CN201062900Y (en) * | 2007-07-30 | 2008-05-21 | 无锡同方人工环境有限公司 | Low temperature air-cooling hot pump system |
CN201885478U (en) * | 2010-12-20 | 2011-06-29 | 天津柯瑞斯空调设备有限公司 | Low temperature type air source heat pump unit |
CN202734344U (en) * | 2012-07-05 | 2013-02-13 | 泰豪科技股份有限公司 | Low temperature enthalpy increasing family type central air conditioner |
CN203443292U (en) * | 2013-07-18 | 2014-02-19 | 成都蓉阳科技有限公司 | Integrated heat-pump drying unit for dehumidification, low-temperature air spraying and enthalpy increase of fresh air of air source |
CN103471275A (en) * | 2013-08-30 | 2013-12-25 | 青岛海信日立空调系统有限公司 | Enhanced vapor injection air-conditioning circulating system and control method thereof |
CN203586601U (en) * | 2013-09-27 | 2014-05-07 | 深圳麦克维尔空调有限公司 | Enhanced-vapour-injection type air-conditioning device |
CN103851828A (en) * | 2014-03-28 | 2014-06-11 | 佛山市顺德区华天成电器有限公司 | Enhanced vapor injection combined system |
CN205316749U (en) * | 2016-01-18 | 2016-06-15 | 山西永有制冷科技有限公司 | Economic ware of freon hydraulic filling formula system's flash distillation bucket |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106969556A (en) * | 2016-12-31 | 2017-07-21 | 广州市粤联水产制冷工程有限公司 | A kind of flash type economizer and cooling cycle system |
CN106969516A (en) * | 2016-12-31 | 2017-07-21 | 广州市粤联水产制冷工程有限公司 | A kind of refrigerating method and cooling cycle system |
CN106705505A (en) * | 2017-02-27 | 2017-05-24 | 莱芜市图腾制冷设备有限公司 | Efficient combined type flash drum pump unit |
CN107677001A (en) * | 2017-09-15 | 2018-02-09 | 北京市京科伦冷冻设备有限公司 | A kind of independent humidification-type fruits and vegetables ice temperature stereo garage carbon dioxide refrigerating system |
CN107677001B (en) * | 2017-09-15 | 2020-02-11 | 北京市京科伦冷冻设备有限公司 | Independent humidification type carbon dioxide refrigerating system for fruit and vegetable ice temperature three-dimensional warehouse |
CN108072190A (en) * | 2017-12-26 | 2018-05-25 | 珠海格力电器股份有限公司 | Air-conditioning system and with its air conditioner |
CN110044132A (en) * | 2019-05-15 | 2019-07-23 | 南京福加自动化科技有限公司 | A kind of propylene full-liquid type refrigeration system and control method |
CN112368528A (en) * | 2019-06-07 | 2021-02-12 | 开利公司 | Modular water side economizer integrated with air cooling chiller |
CN110631281A (en) * | 2019-10-21 | 2019-12-31 | 无锡职业技术学院 | Natural cooling refrigerating system |
Also Published As
Publication number | Publication date |
---|---|
CN105674634B (en) | 2017-12-29 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN105674634A (en) | Freon hydraulic filling type system flashing barrel economizer | |
JP6235467B2 (en) | Condenser / evaporator for cooling device and method thereof | |
CN104154692B (en) | A kind of novel Gas-supplying enthalpy-increasing system and control method thereof | |
CN107014076B (en) | Three-pressure high-efficiency air-cooled heat pump water heater suitable for high-temperature and low-temperature environments | |
CN105258392A (en) | Heat pump heating system, control method and heat pump water heater | |
CN107796146B (en) | Condensing system, air conditioning system and control method | |
CN103398485A (en) | Steam compression refrigerating system device and supercooling method | |
CN104864621B (en) | A kind of four-pipe system Dual-evaporator refrigeration system | |
CN101482321B (en) | Ultra-low temperature heat pump water heater | |
CN110207418A (en) | A kind of heat pump system and control method with double evaporating temperatures | |
CN204739800U (en) | Refrigerating system's four control steam deice structure | |
CN103115452A (en) | Multi-compressor efficient type unit | |
CN205316749U (en) | Economic ware of freon hydraulic filling formula system's flash distillation bucket | |
CN103335440A (en) | Secondary throttling middle complete cooling double-working-condition refrigeration system | |
CN109386980A (en) | A kind of cold and hot energy utility system | |
CN102252412A (en) | Freon-free frequency-conversion air conditioner system | |
CN201615644U (en) | Air-conditioner coolant circulating unit | |
CN102980334A (en) | Refrigerating circuit for use in a motor vehicle | |
CN209355524U (en) | A kind of cold and hot energy utility system | |
CN205066233U (en) | Heat pump heating and heat pump water heater | |
CN209147487U (en) | A kind of low circumstance temperature frequency conversion Air Resource Heat Pump Unit | |
KR101413421B1 (en) | Energy saving freezer and refrigerator by supplying supercooled refrigerant | |
CN105509378B (en) | A kind of automatic evacuation gas device and application method | |
CN103307817B (en) | A kind of vortex parallel Condensing units | |
CN207869575U (en) | Heat pump system |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant |