CN104567054A - Anti-surge system of centrifugal refrigerating unit - Google Patents
Anti-surge system of centrifugal refrigerating unit Download PDFInfo
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- CN104567054A CN104567054A CN201410835276.1A CN201410835276A CN104567054A CN 104567054 A CN104567054 A CN 104567054A CN 201410835276 A CN201410835276 A CN 201410835276A CN 104567054 A CN104567054 A CN 104567054A
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- evaporimeter
- condenser
- water inlet
- refrigerating unit
- prevention system
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 90
- 238000007710 freezing Methods 0.000 claims abstract description 49
- 230000008014 freezing Effects 0.000 claims abstract description 49
- 230000002265 prevention Effects 0.000 claims description 21
- 239000002826 coolant Substances 0.000 claims description 17
- 239000003507 refrigerant Substances 0.000 abstract description 20
- 238000004519 manufacturing process Methods 0.000 abstract 1
- 238000005057 refrigeration Methods 0.000 description 31
- 238000000034 method Methods 0.000 description 9
- 239000000498 cooling water Substances 0.000 description 8
- 238000001704 evaporation Methods 0.000 description 6
- 239000007788 liquid Substances 0.000 description 5
- 238000004781 supercooling Methods 0.000 description 5
- 238000005086 pumping Methods 0.000 description 3
- 230000001276 controlling effect Effects 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 230000001737 promoting effect Effects 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000002596 correlated effect Effects 0.000 description 1
- 230000000875 corresponding effect Effects 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000013526 supercooled liquid Substances 0.000 description 1
Classifications
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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
- 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
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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
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B41/00—Fluid-circulation arrangements
- F25B41/20—Disposition of valves, e.g. of on-off valves or flow control valves
-
- 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
- F25B41/30—Expansion means; Dispositions thereof
-
- 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
- F25B49/00—Arrangement or mounting of control or safety devices
- F25B49/02—Arrangement or mounting of control or safety devices for compression type machines, plants or systems
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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
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2500/00—Problems to be solved
- F25B2500/12—Sound
-
- 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
- F25B2500/00—Problems to be solved
- F25B2500/13—Vibrations
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
- Y02B30/70—Efficient control or regulation technologies, e.g. for control of refrigerant flow, motor or heating
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- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Control Of Positive-Displacement Air Blowers (AREA)
Abstract
The invention relates to the field of anti-surge structures, and discloses an anti-surge system of a centrifugal refrigerating unit, which is characterized in that a compressor and a throttling device are respectively connected between a condenser and an evaporator, and a boosting branch for reducing the pressure difference between the condenser and the evaporator is arranged between the throttling device and a freezing water inlet; the boosting branch circuit comprises a heat exchange device, the heat exchange device is provided with a refrigerant passage and a water passage, the refrigerant passage is communicated with the condenser and the throttling device, the water passage is communicated with the freezing water inlet and the evaporator, and water entering from the freezing water inlet in the heat exchange device exchanges heat with refrigerant coming out of the condenser. Through setting up the branch road that steps up that is used for reducing the pressure differential between condenser and the evaporimeter and set up heat transfer device in the branch road that steps up in this application, effectively reduced the system pressure differential between condenser and the evaporimeter, avoided the problem of the steam bypass valve noise production when opening among the prior art.
Description
Technical field
The present invention relates to anti-surge construction applications, disclose a kind of Surge Prevention System being applied to centrifugal refrigerating unit more specifically.
Background technology
Centrifugal refigerating compressor, as a kind of speed mode compressor, occurs that in running surge phenomenon is its intrinsic a kind of characteristic.Select the refrigeration central air-conditioner unit of centrifugal compressor, in its design and actual use procedure, all will note the generation avoiding surge phenomenon the moment.
The mechanism that in compressor operating process, surge phenomenon occurs is roughly divided into two classes: one is High Pressure Difference; Two is low discharges.Because above-mentioned two factors cause the entry guide vane adjusting gas flow of Compressor Group in compressor operating process and the motor speed of frequency converter sets to regulate, all need the appearance in order to avoid surge phenomenon and carry out suitable restriction, therefore limiting the actual motion scope of Compressor Group to a certain extent.
Simultaneously, when centrifugal refigerating compressor because cooling tower scarce capacity causes the water temperature of cooling water higher, thus cause condensing pressure to exceed unit design pressure, or because actual load is lower than situations such as unit capacity adjustment lower limit cause freezing temperature on the low side, all surge phenomenon can be there is by induced to compressor unit.
The way solving surge in centrifugal compressors phenomenon in prior art is install hot gas bypass valve in compressor bank mostly.When predicting compressor bank generation surge phenomenon, conducting is carried out by opening hot gas bypass valve, the refrigerant gas of HTHP is directly ganged up and is entered evaporimeter, the height pressure reduction of reduction system, increase the suction tolerance of compressor simultaneously, make Compressor Group away from pumping point, but there are the following problems for this control method: the gaseous refrigerant of (1) HTHP enters evaporimeter with high flow velocity, with larger noise; (2) the suction tolerance increase of compressor causes power consumption to increase, but does not have refrigeration because of the gaseous coolant of coming from condenser bypass, and compressor causes the waste in resource to its acting, the service behaviour coefficient of compressor is had a greatly reduced quality; (3) affect by factors such as magnetic valve specification and bypass line calibers, the hot-gas bypass amount of Compressor Group is limited, for relatively large unit, the effect proportion of hot-gas bypass can reduce, and adopts the scheme of above-mentioned installation by-passing valve to the often just an utterly inadequate amount of the working condition of whole Compressor Group.
Therefore, in order to meet the needs of centrifugal refrigerating unit prevention surge phenomenon, under a kind of condition not affecting economy is needed in market badly, the critical data that the sensor can be correlated with by refrigeration unit is detected, by promoting evaporating pressure to expand the method for compressor operating scope before surge phenomenon occurs, make refrigeration unit away from the centrifugal refrigerating unit Surge Prevention System of surge phenomenon.
Summary of the invention
One object of the present invention is, under the condition not affecting centrifugal refrigerating unit performance driving economy, a kind of centrifugal refrigerating unit Surge Prevention System is proposed, when centrifugal refrigerating unit works under the operating mode of Smaller load, High Pressure Difference, effectively can prevent the phenomenon of centrifugal refrigerating unit generation surge, effectively improve and promote the energy efficiency circular of centrifugal refrigerating unit.
For reaching this object, the present invention by the following technical solutions:
A kind of centrifugal refrigerating unit Surge Prevention System, is connected to compressor and throttling arrangement, is provided with the boosting branch road for reducing pressure differential between described condenser and evaporimeter between described throttling arrangement and freezing water inlet between condenser and evaporimeter; Containing heat-exchanger rig in described boosting branch road, there is in described heat-exchanger rig coolant path and water passage, described coolant path is communicated with described condenser and throttling arrangement, described water passage is communicated with described freezing water inlet and evaporimeter, and the water entered from described freezing water inlet in described heat-exchanger rig carries out heat exchange with cold-producing medium out from described condenser.
Further, three-way diverter valve is provided with between described freezing water inlet and described evaporimeter; Three valve ports of described three-way diverter valve are connected with the water inlet pipe of boosting branch road with freezing water inlet, evaporimeter respectively.
Further, described boosting branch road comprises heat exchanger, outlet pipe and described water inlet pipe; The coolant path of described heat exchanger connects described condenser and described throttling arrangement, and between the water passage that described outlet pipe is connected to described heat exchanger and evaporimeter, described water inlet pipe is connected between described three-way diverter valve and the water passage of heat exchanger.
Further, also comprise control device, described control device for control described three-way diverter valve three valve ports between commutation and aperture.
Further, the temperature sensor of the water temperature for detecting the water flowing into and flow out described evaporimeter is also comprised, for detecting the pressure sensor of the working pressure of described evaporimeter and condenser and the current transformer for detecting size of current in described compressor.
Further, described control device be connected with described temperature sensor, pressure sensor summation current transformer respectively.
Preferably, described three-way diverter valve is electric three passes reversal valve.
Preferably, described heat exchanger is plate type heat exchanger.
Preferably, described throttling arrangement is choke valve.
Beneficial effect of the present invention is: in the application by arrange for reducing the pressure differential between condenser and evaporimeter boosting branch road and boosting branch road in heat-exchanger rig is set, heat-exchanger rig has coolant path and water passage, coolant path is communicated with condenser and throttling arrangement, water passage is communicated with freezing water inlet and evaporimeter, the water entered from freezing water inlet in heat-exchanger rig carries out heat exchange with cold-producing medium out from condenser, effectively reduce the system pressure difference between condenser and evaporimeter, avoid the noise that hot gas bypass valve of the prior art produces when opening.
A closed circulation system is formed between boosting branch road and evaporimeter, evaporimeter can also be entered into continue to be used after water in boosting branch road and refrigerant heat exchanger, for the water cleaning of heat exchange, compared with hot gas bypass valve in prior art, the plate type heat exchanger life-span used in the application is longer, economic benefit is better, and dependability is higher.
By promoting the degree of supercooling of evaporating temperature in evaporimeter and refrigerant in the application, the efficiency of refrigeration unit can also be promoted to a certain extent while in use there is surge phenomenon to prevent centrifugal refrigerating unit, avoid the waste of resource and the energy using hot gas bypass valve to bring in prior art, make the utilization rate of energy in the heat transfer process of refrigeration unit higher.
Accompanying drawing explanation
Fig. 1 is the Integral connection structure schematic diagram of the centrifugal refrigerating unit Surge Prevention System that the specific embodiment of the invention proposes;
Fig. 2 is the surge Forecast curve of the Surge Prevention System that the specific embodiment of the invention proposes.
In figure:
1, condenser; 2, evaporimeter; 3, compressor; 4, throttling arrangement; 5, heat exchanger; 6, three-way diverter valve; 7, freezing water inlet; 8, freezing delivery port; 9, cooling water outlet mouth; 10, coolant intake; 11, water inlet pipe; 12, outlet pipe; 13, control device.
Detailed description of the invention
Technical scheme of the present invention is further illustrated by detailed description of the invention below in conjunction with accompanying drawing.
As shown in Figure 1, be the concrete syndeton of centrifugal refrigerating unit Surge Prevention System that the specific embodiment of the invention proposes.Connected mode between all parts in refrigeration unit in the present invention is roughly the same with the connected mode of refrigeration unit of the prior art, comprises condenser 1 and evaporimeter 2, is connected to compressor 3 and throttling arrangement 4 between condenser 1 and evaporimeter 2.Condenser 1 is connected with cooling water outlet mouth 9 and coolant intake 10, coolant intake 10 is for entering into condenser 1 for extraneous cooling water and carry out heat exchange with the cold-producing medium of condenser 1, and cooling water outlet mouth 9 is for being discharged in external environment from condenser 1 for the cooling water after heat exchange.Evaporimeter 2 is connected with freezing water inlet 7 and freezing delivery port 8, freezing water inlet 7 for passing into for carrying out the water of heat exchange with cold-producing medium in evaporimeter 2, and freezing delivery port 8 is for being expelled to the water after heat exchange outside evaporimeter 2 from evaporimeter 2.Cooling water inlet 10 and between coolant outlet 9 and condenser, and freezing water inlet 7 and being all connected by pipeline between freezing delivery port 8 with evaporimeter 2.
Using hot gas bypass valve to prevent refrigeration unit to occur surge phenomenon and the various problems that cause to solve in prior art, between throttling arrangement 4 and freezing water inlet 7, in the present invention, being provided with the boosting branch road for reducing pressure differential between condenser 1 and evaporimeter 2.Containing heat-exchanger rig in boosting branch road, heat-exchanger rig has coolant path and water passage, coolant path is communicated with condenser 1 and throttling arrangement 4, water passage is communicated with freezing water inlet 7 and evaporimeter 2, and the water entered from freezing water inlet 7 in heat-exchanger rig carries out heat exchange with cold-producing medium out from condenser 1.
Boosting branch road comprises heat exchanger 5, outlet pipe 12 and water inlet pipe 11, heat exchanger 5 is arranged between condenser 1 and throttling arrangement 4, the coolant path of heat exchanger 5 connects condenser 1 and throttling arrangement 4, outlet pipe is connected between the water passage of heat exchanger 5 and evaporimeter 2, and the liquid refrigerants out entering into the coolant path of heat exchanger 5 from condenser 1 needs first after heat exchanger 5 carries out heat exchange, to enter into throttling arrangement 4 again.The outlet of the water passage of heat exchanger 5 is connected by outlet pipe 12 with between evaporimeter 2, is connected between three-way diverter valve 6 with heat exchanger 5 by water inlet pipe 11.In the present invention, heat-exchanger rig is heat exchanger 5, and as the preferred embodiment of one, plate type heat exchanger selected by the heat exchanger 5 in the present embodiment, and the throttling arrangement 4 in the present embodiment is choke valve.
Centrifugal refrigerating unit Surge Prevention System in the present embodiment also comprises control device 13, control device 13 for control three-way diverter valve 6 three valve ports between commutation and aperture.More specifically, three valve ports of three-way diverter valve 6 are connected with the water inlet pipe 11 of freezing water inlet 7, evaporimeter 2 and the branch road that boosts respectively.Control device 13 can realize the connection between freezing water inlet 7 and condenser 1 by the opening and closing controlling three-way diverter valve 6 three valve ports, or realizes the connection between freezing water inlet 7 and heat exchanger 5.Control device 13 can also control the flow of the water passed through between any two valve ports of three-way diverter valve 6 according to situation about occurring in use procedure.Control device 13 can adopt PLC to control, but control device 13 is not limited to above-mentioned a kind of control mode, can also adopt other control mode.Three-way diverter valve 6 in the present embodiment is electric three passes reversal valve, and control device 13 is electrically connected with three-way diverter valve 6 and controls.
In order to detecting in the Surge Prevention System course of work and preventing, also comprise the temperature sensor of the water temperature for detecting the water flowing into and flow out evaporimeter 2 in the present embodiment, for detecting the pressure sensor of the working pressure of evaporimeter 2 and condenser 1 and the current transformer for detecting size of current in compressor 3.Concrete, freezing water inlet 7 position is provided with the first temperature sensor, and freezing delivery port 8 position is provided with the second temperature sensor; Condenser 1 is provided with the first pressure sensor, evaporimeter 2 is provided with the second pressure sensor; Compressor 3 is provided with current transformer.Force value on the condenser 1 that first pressure sensor detects is P1, and the force value on the evaporimeter 2 that the second pressure sensor detects is P2; The temperature that first temperature sensor detects freezing water inlet 7 position is T1, and the temperature that the second temperature sensor detects freezing delivery port 8 position is T2, and the size of current that current transformer detects on compressor 3 is A.Control device 13 is connected with temperature sensor, pressure sensor summation current transformer respectively.While the parameters value collected each temperature sensor above-mentioned, pressure sensor summation current transformer processes, each sensor is controlled.By detecting the water temperature of freezing water inlet 7 and freezing delivery port 8 and obtaining water temperature difference to judge the load in refrigeration unit running.By detecting the pressure in evaporimeter 2 and condenser 1 course of work and obtaining pressure differential to prevent the generation of surge in the refrigeration unit course of work, and take corresponding anti-surge measure, make refrigeration unit away from pumping point, pre-anti-surge occurs.Obtain current fluctuation by carrying out detection to the electric current in compressor 3 course of work, accurately to judge whether surge has occurred and taken measures in time, can not be damaged to protect refrigeration unit.
Temperature difference Δ T=│ T1-T2 │ between freezing water inlet 7 and freezing delivery port 8, the pressure difference value between condenser 1 and evaporimeter 2 is Δ P=│ P1-P2 │.Prediction regulation line for surge by being formed between Δ T and Δ P in the present invention is predicted the situation that surge will occur refrigeration unit, and before actual surge phenomenon occurs, to heat exchanger 5, a certain amount of freezing water inlet is introduced from freezing water inlet 7 by the open and-shut mode of three valve ports controlling three-way diverter valve 6, the high-temperature liquid state refrigerant formed in heat exchanger 5 before freezing water inlet and throttling carries out heat exchange, and the water heated up after heat exchange is incorporated in evaporimeter 2 by outlet pipe 12, to avoid occurring surge phenomenon in actual use.Adopt aforesaid way, can promote the evaporating pressure of evaporimeter 2 on the one hand, the range of operation of expansion compressor 3, makes refrigeration unit away from pumping point, there will not be surge phenomenon; On the other hand, the degree of supercooling of the refrigerant before can increasing throttling, the efficiency of effective elevator system is higher to the utilization ratio of refrigerant.
Syndeton as shown in Figure 2 in composition graphs 1, by to determining frequency or frequency conversion refrigeration unit is tested in the present embodiment, by the water temperature difference Δ T that detects between freezing water inlet 7 and freezing delivery port 8 and the pressure differential Δ P obtained between evaporimeter 2 and condenser 1 thus the surge Forecast curve of the Surge Prevention System obtained.Can learn from figure, along with the increase of temperature difference Δ T, namely the flow of compressor 3 increases gradually, then prediction curve is more away from surging condition point, and higher height pressure differential deltap P can be obtained, therefore can predict the surge condition of refrigeration unit in real work according to the prediction regulation line for surge in figure.
In the process that refrigeration unit is controlled, before the actual surge line of refrigeration unit evaporimeter 2 Inlet and outlet water temperature difference T and refrigeration unit system height pressure differential deltap P, reserved certain control surplus, under certain Δ T being detected, the height pressure reduction of refrigeration unit system has exceeded prediction regulation line for surge, the valve port of three-way diverter valve 6 that then control device 13 controls between evaporimeter 2 and freezing water inlet 7 is changed, the part in the low-temperature cooling water entered from freezing water inlet 7 is incorporated in heat exchanger 5 with throttling before high-temperature liquid state refrigerant carry out heat exchange.
Refrigerant after heat exchanger heat exchange cooling obtains larger degree of supercooling, structure in above-mentioned boosting branch road can take different arrangement forms according to the difference of refrigerating unit structure, for refrigeration unit be single-stage circulation system architecture directly can enter into evaporimeter after throttling arrangement throttling.For multiple stage circulation refrigeration unit, before heat exchanger can be arranged in one-level throttling, cooled supercooled liquid refrigerant enters flash evaporation after throttling.Also, before heat exchanger can being arranged in two-step throttle, the liquid refrigerants of being drawn by flash evaporation enters after heat exchanger heat exchange obtains degree of supercooling, then goes to evaporimeter via second throttle.
If after taking above-mentioned measure; refrigeration unit condition of work is more severe; namely the chilled water entered from freezing water inlet 7 be all introduced in heat exchanger 5 with throttling before refrigerant carry out heat exchange; when refrigeration unit still cannot exit Anti-surge Control; whether the fluctuation situation of electric current then detected according to the current transformer that compressor 3 is arranged exceedes enable state judges that whether refrigeration unit is actual surge occurs, and takes stoppage protection measure.
According to the parameter that each sensor arranged in refrigeration unit collects, and the antisurge control line preset, judge the degree of closeness of the state that refrigeration unit is run and surging condition, control the aperture of three-way diverter valve, the freezing water inlet part or all entered from freezing water inlet is incorporated in heat exchanger, flow back into again in evaporimeter after the heat exchange carried out in advance of chilled water in heat exchanger and high temperature refrigerant heats up, improve refrigeration unit evaporating pressure and reduce operation pressure ratio, make compressor operating pressure ratio condition milder, refrigeration unit can be offloaded to less load range with closing to reality situation.On the other hand, high-temperature liquid state refrigerant, after heat exchange, obtains larger degree of supercooling, and the restriction loss that the refrigerant carrying out throttling again after heat exchange produces is fewer, and the utilization ratio of evaporimeter to refrigerant is higher, and the efficiency of refrigeration unit obtains and increases substantially.
In the application by arrange for reducing the pressure differential between condenser and evaporimeter boosting branch road and boosting branch road in heat-exchanger rig is set, the water entered from freezing water inlet in heat-exchanger rig carries out heat exchange with cold-producing medium out from condenser, effectively reducing the system pressure difference between condenser and evaporimeter, avoiding the noise that hot gas bypass valve of the prior art produces when opening.
Below describe know-why of the present invention in conjunction with specific embodiments, these describe just in order to explain principle of the present invention, can not be interpreted as limiting the scope of the invention by any way.Based on explaining herein, those skilled in the art does not need to pay performing creative labour can associate other detailed description of the invention of the present invention, and these modes all will fall within protection scope of the present invention.
Claims (9)
1. a centrifugal refrigerating unit Surge Prevention System, be connected to compressor (3) and throttling arrangement (4) between condenser (1) and evaporimeter (2), it is characterized in that: between described throttling arrangement (4) and freezing water inlet (7), be provided with the boosting branch road for reducing pressure differential between described condenser (1) and evaporimeter (2);
Containing heat-exchanger rig in described boosting branch road, described heat-exchanger rig has coolant path and water passage, described coolant path is communicated with described condenser (1) and throttling arrangement (4), described water passage is communicated with described freezing water inlet (7) and evaporimeter (2), the water entered from described freezing water inlet (7) in described heat-exchanger rig and from described condenser (1) cold-producing medium out carry out heat exchange.
2. centrifugal refrigerating unit Surge Prevention System according to claim 1, is characterized in that: be provided with three-way diverter valve (6) between described freezing water inlet (7) and described evaporimeter (2);
Three valve ports of described three-way diverter valve (6) are connected with the water inlet pipe (11) of the branch road that boosts with freezing water inlet (7), evaporimeter (2) respectively.
3. centrifugal refrigerating unit Surge Prevention System according to claim 2, is characterized in that: described boosting branch road comprises heat exchanger (5), outlet pipe (12) and described water inlet pipe (11);
The coolant path of described heat exchanger (5) connects described condenser (1) and throttling arrangement (4), described outlet pipe is connected between the water passage of described heat exchanger (5) and evaporimeter (2), and described water inlet pipe (11) is connected between the water passage of described three-way diverter valve (6) and heat exchanger (5).
4. the centrifugal refrigerating unit Surge Prevention System according to Claims 2 or 3, it is characterized in that: also comprise control device (13), described control device (13) for control described three-way diverter valve three valve ports between commutation and aperture.
5. centrifugal refrigerating unit Surge Prevention System according to claim 4, is characterized in that: also comprise the temperature sensor of the water temperature for detecting the water flowing into and flow out described evaporimeter (2), for detecting the pressure sensor of the working pressure of described evaporimeter (2) and condenser (1) and the current transformer for detecting size of current in described compressor (3).
6. centrifugal refrigerating unit Surge Prevention System according to claim 5, is characterized in that: described control device (13) is connected with described temperature sensor, pressure sensor summation current transformer respectively.
7. the centrifugal refrigerating unit Surge Prevention System according to any one of claim 1-3, is characterized in that: described three-way diverter valve (6) is electric three passes reversal valve.
8. centrifugal refrigerating unit Surge Prevention System according to claim 3, is characterized in that: described heat exchanger (5) is plate type heat exchanger.
9. the centrifugal refrigerating unit Surge Prevention System according to any one of claim 1-3, is characterized in that: described throttling arrangement (4) is choke valve.
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| CN201410835276.1A CN104567054B (en) | 2014-12-26 | 2014-12-26 | Anti-surge system of centrifugal refrigerating unit |
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| CN201410835276.1A CN104567054B (en) | 2014-12-26 | 2014-12-26 | Anti-surge system of centrifugal refrigerating unit |
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| CN104567054B CN104567054B (en) | 2017-05-03 |
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| CN107830662A (en) * | 2017-10-30 | 2018-03-23 | 珠海格力电器股份有限公司 | Control method and system of centrifugal water chilling unit |
| CN109654762A (en) * | 2017-10-12 | 2019-04-19 | 荏原冷热系统株式会社 | Centrifugal refrigerator |
| CN112050490A (en) * | 2020-09-25 | 2020-12-08 | 浙江国祥股份有限公司 | Evaporative cooling centrifugal water chilling unit |
| CN113959131A (en) * | 2021-10-08 | 2022-01-21 | 青岛海尔空调电子有限公司 | Method and device for controlling water chilling unit and water chilling unit |
| CN114413457A (en) * | 2022-01-21 | 2022-04-29 | 清华大学 | Optimization control method and device for air conditioning system, electronic equipment and storage medium |
| CN115398159A (en) * | 2020-02-28 | 2022-11-25 | 江森自控泰科知识产权控股有限责任合伙公司 | System with automatic cooler antisurge and method of operating a cooler to avoid future surge events |
| CN116659109A (en) * | 2023-07-25 | 2023-08-29 | 浙江科维节能技术股份有限公司 | Anti-surge ammonia refrigeration system for ammonia synthesis device and anti-surge method thereof |
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| CN109654762A (en) * | 2017-10-12 | 2019-04-19 | 荏原冷热系统株式会社 | Centrifugal refrigerator |
| CN107830662A (en) * | 2017-10-30 | 2018-03-23 | 珠海格力电器股份有限公司 | Control method and system of centrifugal water chilling unit |
| CN107830662B (en) * | 2017-10-30 | 2019-10-08 | 珠海格力电器股份有限公司 | Control method and system of centrifugal water chilling unit |
| CN115398159A (en) * | 2020-02-28 | 2022-11-25 | 江森自控泰科知识产权控股有限责任合伙公司 | System with automatic cooler antisurge and method of operating a cooler to avoid future surge events |
| CN112050490A (en) * | 2020-09-25 | 2020-12-08 | 浙江国祥股份有限公司 | Evaporative cooling centrifugal water chilling unit |
| CN113959131A (en) * | 2021-10-08 | 2022-01-21 | 青岛海尔空调电子有限公司 | Method and device for controlling water chilling unit and water chilling unit |
| CN114413457A (en) * | 2022-01-21 | 2022-04-29 | 清华大学 | Optimization control method and device for air conditioning system, electronic equipment and storage medium |
| CN116659109A (en) * | 2023-07-25 | 2023-08-29 | 浙江科维节能技术股份有限公司 | Anti-surge ammonia refrigeration system for ammonia synthesis device and anti-surge method thereof |
| CN116659109B (en) * | 2023-07-25 | 2023-10-17 | 浙江科维节能技术股份有限公司 | Anti-surge ammonia refrigeration system for ammonia synthesis device and anti-surge method thereof |
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