CN106403453A - Zero discharge type circulating water cooling system - Google Patents
Zero discharge type circulating water cooling system Download PDFInfo
- Publication number
- CN106403453A CN106403453A CN201611036409.4A CN201611036409A CN106403453A CN 106403453 A CN106403453 A CN 106403453A CN 201611036409 A CN201611036409 A CN 201611036409A CN 106403453 A CN106403453 A CN 106403453A
- Authority
- CN
- China
- Prior art keywords
- cooling system
- cooler
- circulating water
- zero
- extender
- 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.)
- Pending
Links
- 238000001816 cooling Methods 0.000 title claims abstract description 224
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 148
- 239000000498 cooling water Substances 0.000 claims abstract description 70
- 239000004606 Fillers/Extenders Substances 0.000 claims description 65
- 239000003507 refrigerant Substances 0.000 claims description 63
- 239000006200 vaporizer Substances 0.000 claims description 36
- 239000003795 chemical substances by application Substances 0.000 claims description 28
- 238000004891 communication Methods 0.000 claims description 21
- 239000007788 liquid Substances 0.000 claims description 21
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical group N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims description 20
- 230000001351 cycling effect Effects 0.000 claims description 20
- 239000006096 absorbing agent Substances 0.000 claims description 16
- 230000008676 import Effects 0.000 claims description 16
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 claims description 15
- 238000007906 compression Methods 0.000 claims description 13
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 10
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 claims description 10
- 229910021529 ammonia Inorganic materials 0.000 claims description 10
- 230000006835 compression Effects 0.000 claims description 10
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 10
- AMXOYNBUYSYVKV-UHFFFAOYSA-M lithium bromide Chemical compound [Li+].[Br-] AMXOYNBUYSYVKV-UHFFFAOYSA-M 0.000 claims description 6
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 claims description 5
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims description 5
- 239000005977 Ethylene Substances 0.000 claims description 5
- 239000001273 butane Substances 0.000 claims description 5
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 claims description 5
- 229910052757 nitrogen Inorganic materials 0.000 claims description 5
- 239000001294 propane Substances 0.000 claims description 5
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 claims description 5
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 claims description 5
- 238000011144 upstream manufacturing Methods 0.000 claims description 3
- 239000007789 gas Substances 0.000 claims description 2
- 230000000694 effects Effects 0.000 abstract description 20
- 239000002351 wastewater Substances 0.000 abstract description 17
- 239000002826 coolant Substances 0.000 abstract description 10
- 239000003638 chemical reducing agent Substances 0.000 abstract 1
- 238000005057 refrigeration Methods 0.000 description 15
- 239000007791 liquid phase Substances 0.000 description 10
- 238000000034 method Methods 0.000 description 8
- 230000008901 benefit Effects 0.000 description 7
- 230000007613 environmental effect Effects 0.000 description 7
- 230000002950 deficient Effects 0.000 description 5
- 238000010586 diagram Methods 0.000 description 5
- 230000008569 process Effects 0.000 description 5
- 125000004122 cyclic group Chemical group 0.000 description 4
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 4
- 239000002440 industrial waste Substances 0.000 description 4
- 239000013589 supplement Substances 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 3
- 230000000295 complement effect Effects 0.000 description 3
- 238000009833 condensation Methods 0.000 description 3
- 230000005494 condensation Effects 0.000 description 3
- 230000006837 decompression Effects 0.000 description 3
- 230000007423 decrease Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- 239000012808 vapor phase Substances 0.000 description 3
- 230000005611 electricity Effects 0.000 description 2
- 238000004134 energy conservation Methods 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 241000937378 Everettia interior Species 0.000 description 1
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 description 1
- 229910019142 PO4 Inorganic materials 0.000 description 1
- 150000001335 aliphatic alkanes Chemical class 0.000 description 1
- 230000000844 anti-bacterial effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 230000008602 contraction Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 229910052731 fluorine Inorganic materials 0.000 description 1
- 239000011737 fluorine Substances 0.000 description 1
- 239000013505 freshwater Substances 0.000 description 1
- 238000002309 gasification Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 230000002045 lasting effect Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 1
- 239000010452 phosphate Substances 0.000 description 1
- 230000008439 repair process Effects 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 210000000582 semen Anatomy 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 238000003809 water extraction Methods 0.000 description 1
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
- F25D—REFRIGERATORS; COLD ROOMS; ICE-BOXES; COOLING OR FREEZING APPARATUS NOT OTHERWISE PROVIDED FOR
- F25D17/00—Arrangements for circulating cooling fluids; Arrangements for circulating gas, e.g. air, within refrigerated spaces
- F25D17/02—Arrangements for circulating cooling fluids; Arrangements for circulating gas, e.g. air, within refrigerated spaces for circulating liquids, e.g. brine
-
- 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
- F25B43/00—Arrangements for separating or purifying gases or liquids; Arrangements for vaporising the residuum of liquid refrigerant, e.g. by heat
-
- 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
- F25B9/00—Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point
- F25B9/06—Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point using expanders
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Analytical Chemistry (AREA)
- Power Engineering (AREA)
- Other Air-Conditioning Systems (AREA)
Abstract
The invention discloses a zero discharge type circulating water cooling system and relates to the technical field of cooling. The circulating water cooling system comprises an inner circulating cooling system and an outer circulating cooling system for providing cooling capacity for the inner circulating cooling system; a working medium of the inner circulating cooling system is cooling water; the inner circulating cooling system comprises a circulating water pipeline, a first cooler for cooling a thermal medium, a second cooler for cooling the cooling water as well as a circulating pump for driving the cooling water to flow in the circulating water pipeline, and the first cooler, the second cooler and the circulating pump are mounted on the circulating water pipeline; a working medium of the outer circulating cooling system is a coolant; and the outer circulating cooling system comprises a coolant circulating pipeline as well as a coolant circulating device, a coolant cooler and a pressure reducer which are mounted on the coolant circulating pipeline. The system has the good and stable cooling effect, can realize zero discharge of waste water, is environment-friendly and can save water resources and the cost.
Description
Technical field
The present invention relates to cooling technology field, in particular to a kind of zero-emission type circulating water cooling system.
Background technology
For cooling technology field, because the used heat of factory is more, need substantial amounts of recirculated cooling water, such as using conventional work
Skill, then the consumption of raw water and the discharge capacity of waste water are huge, and water rate and cost of water treatment are high.
Additionally, being limited to the raw material place of production, some factories typically build in northwest water-deficient area, substantial amounts of water demand
Make plant condition harsh.
In today that water resource is day by day in short supply, huge water consumption seriously hinders and constrains the development of enterprise.Although it is big
Cooling water is changed to recirculated cooling water by Some Enterprises, but it is still very big to supplement fresh water amount.
Generally 30 DEG C～35 DEG C of existing circulating water cooling system inflow temperature, for preventing equipment serious scale, backwater temperature
Below 50 DEG C, this leads to cooling circulating water amount very big to degree temperature general control, and its water consumption accounts for the 85%- of enterprise water use
92%, power load accounts for the 20%-30% of total electricity consumption.And the increase with cycle-index, water quality deterioration, hardness uprises, and holds
Easy occluding device pipeline simultaneously makes cooling effect substantially reduce, and needs persistently discharge recirculated water, and supplements substantial amounts of new recirculated water, sternly
Weight waste water resource.The antisludging agent that contains in recirculated water, antibacterial, such as phosphate etc., outside undressed recirculated water, row will be right
Environment does great damage.
With the increasingly stringent of environmental requirement, recycling waste water discharge has become the emphasis of each environmental protection of enterprise regulation, each land
Explicit order newly-built enterprise in mansion must realize wastewater zero discharge, but carries out zero to the recirculated cooling water waste water in existing cooling system
Discharge transformation, need to carry out permeating, the technique salt extraction such as concentrate, evaporate, being dried, greatly increase the operating cost of circulating cooling system.
In addition, in regular circulation technique, using shell-and-tube heat exchanger, cooler is made up of multiple heat exchangers, is
Consider that what circulating water cooling system ran is uniformly coordinated, and prevent high-temperature scaling, cooling water enters the temperature one of each cooler
As be 30 DEG C～32 DEG C, go out generally 40 DEG C～42 DEG C of the temperature of each cooler, only 10 DEG C of cooling water temperature rise, under same load,
Temperature rise is less, and circulating load is bigger, and the volume of equipment and investment are all very big.
Content of the invention
It is an object of the invention to provide a kind of zero-emission type circulating water cooling system, its good refrigeration effect and refrigeration
Stable, wastewater zero discharge, environmental friendliness, saving water resource and operating cost.
Embodiments of the invention are realized in：
A kind of zero-emission type circulating water cooling system, it includes interior circulation cooling system and is used for as interior circulation cooling system
The external circulation cooling system of cold is provided.The working media of interior circulation cooling system is cooling water, and interior circulation cooling system includes
Circulating water line and be installed on circulating water line the first cooler for cooling down thermal medium, for cool down cooling water the
Two coolers and the circulating pump for driving cooling water to flow in circulating water line.The working media of external circulation cooling system is
Cold-producing medium, external circulation cooling system includes refrigerant circulation line and the refrigerant cycle dress being installed on refrigerant circulation line
Put, refrigerant cooler and decompressor.
Further, in the preferred embodiment of the present invention, according to cooling water circulating water line flow direction, second is cold
But the upstream of device is additionally provided with air precooler.
Further, in the preferred embodiment of the present invention, refrigerant cycle apparatus include compressor, the second cooler
Refrigerant outlet and compressor inlet communication, the outlet of compressor and the inlet communication of refrigerant cooler.
Further, in the preferred embodiment of the present invention, cold-producing medium be ammonia, nitrogen, methane, ethane, ethylene, third
Any one in alkane, propylene, butane, pentane and freon.
Further, in the preferred embodiment of the present invention, refrigerant cycle apparatus include absorber, solution pump and use
In the generator carrying out heat exchange with thermal medium, cold-producing medium is absorbing liquid and combining of circulating agent.The outlet of the second cooler with
The inlet communication of absorber, the outlet of absorber is connected by solution pump with the import of generator, the refrigerant outlet of generator with
The inlet communication of refrigerant cooler, the absorbing liquid outlet of generator and the absorbing liquid inlet communication of absorber.
Further, in the preferred embodiment of the present invention, absorbing liquid is water and circulates agent for ammonia；Or absorbing liquid is
Lithium bromide and circulate agent be water.
Further, in the preferred embodiment of the present invention, external circulation cooling system also includes extender cycling element；
The working media of extender cycling element is extender.Extender cycling element includes decompressor, extender cooler, booster pump
With the vaporizer carrying out heat exchange for extender and thermal medium.The outlet of decompressor and the inlet communication of extender cooler,
The outlet of extender cooler is connected by booster pump with the extender entrance of vaporizer, and the extender of vaporizer exports and decompressor
Inlet communication；The power output portion of decompressor is connected with the compression power input unit of compressor.
Further, in the preferred embodiment of the present invention, external circulation cooling system also includes extender cycling element；
Extender cycling element includes decompressor, booster pump and the vaporizer carrying out heat exchange for extender and thermal medium；Decompressor
Outlet and refrigerant cooler inlet communication, the extender import of vaporizer and the outlet of refrigerant cooler are by booster pump
Connection, the extender outlet of vaporizer is connected with expander inlet；The power output portion of decompressor and the compression power of compressor
Input unit connects.
Further, in the preferred embodiment of the present invention, it is provided between vaporizer and the first cooler and is situated between for heat
The arm that matter is passed through, arm connects the thermal medium outlet of vaporizer and the thermal medium inlet of the first cooler.
Further, in the preferred embodiment of the present invention, the first cooler is plate-fin heat exchanger.
The beneficial effect of the embodiment of the present invention is：By arranging the interior circulation cooling system matching and outer circulation cooling system
System, the cooling water of external circulation cooling system inner loop cooling system has cooling effect again so that interior circulation cooling system can
To provide enough colds for thermal medium, improve the cooling effect to thermal medium for the interior circulation cooling system.
Because external circulation cooling system inner loop cooling system has cooling Stabilization so that interior circulation cooling system
Cooling water can be adequately cooled after providing cold for thermal medium and supplement sufficient cold, interior circulation can be made
Cooling system, in the case of lasting cooling work, still ensures that interior circulation cooling system has normal refrigeration, improves
The overall refrigeration stability of zero-emission type circulating water cooling system.Further, since zero-emission type circulating water cooling system is overall
For circulating cooling, circulating water uses, and greatly reduces the consumption of cooling water, saving water resource and operating cost；And it is cold
But water is recycled due to repeatable, can reach wastewater zero discharge, prevent the pollution of the environment.
The zero-emission type circulating water cooling system being provided using the application, can greatly reduce cooling water water consumption, and can
Reach wastewater zero discharge, prevent from polluting, make water-deficient area and the high area of environmental requirement also can meet plant condition.
Brief description
In order to be illustrated more clearly that the technical scheme of the embodiment of the present invention, below will be attached to use required in embodiment
Figure is briefly described it will be appreciated that the following drawings illustrate only certain embodiments of the present invention, and it is right to be therefore not construed as
The restriction of scope, for those of ordinary skill in the art, on the premise of not paying creative work, can also be according to this
A little accompanying drawings obtain other related accompanying drawings.
The schematic diagram of the zero-emission type circulating water cooling system that Fig. 1 provides for the embodiment of the present invention 1；
The schematic diagram of the zero-emission type circulating water cooling system that Fig. 2 provides for the embodiment of the present invention 2；
First cooler of the zero-emission type circulating water cooling system that Fig. 3 provides for the embodiment of the present invention 2 is changed by shell-and-tube
Schematic diagram after hot device replacement；
The schematic diagram of the zero-emission type circulating water cooling system that Fig. 4 provides for the embodiment of the present invention 3；
The schematic diagram of the zero-emission type circulating water cooling system that Fig. 5 provides for the embodiment of the present invention 4.
Icon：100- zero-emission type circulating water cooling system；110- interior circulation cooling system；111- circulating water line；
112- first cooler；113- second cooler；114- circulating pump；115- air precooler；120- external circulation cooling system；
121- refrigerant circulation line；122- refrigerant cycle apparatus；122a- compressor；123- refrigerant cooler；124- reduces pressure
Device；200- zero-emission type circulating water cooling system；220- external circulation cooling system；222- extender cycling element；222a- expands
Machine；222b- extender cooler；222c- booster pump；222d- vaporizer；300- zero-emission type circulating water cooling system；320-
External circulation cooling system；322- extender cycling element；322a- decompressor；322b- booster pump；322c- vaporizer；324- props up
Pipe；400- zero-emission type circulating water cooling system；420- external circulation cooling system；422- refrigerant cycle apparatus；422a- absorbs
Device；422b- solution pump；422c- generator.
Specific embodiment
Purpose, technical scheme and advantage for making the embodiment of the present invention are clearer, below in conjunction with the embodiment of the present invention
In accompanying drawing, the technical scheme in the embodiment of the present invention is clearly and completely described it is clear that described embodiment is
The a part of embodiment of the present invention, rather than whole embodiments.The present invention generally described and illustrated in accompanying drawing herein is implemented
The assembly of example can be arranged with various different configurations and design.
Therefore, below the detailed description of the embodiments of the invention providing in the accompanying drawings is not intended to limit claimed
The scope of the present invention, but be merely representative of the selected embodiment of the present invention.Based on the embodiment in the present invention, this area is common
The every other embodiment that technical staff is obtained under the premise of not making creative work, broadly falls into the model of present invention protection
Enclose.
It should be noted that：Similar label and letter represent similar terms in following accompanying drawing, therefore, once a certain Xiang Yi
It is defined in individual accompanying drawing, then do not need it to be defined further and explains in subsequent accompanying drawing.
Embodiment 1
Refer to Fig. 1, present embodiments provide a kind of zero-emission type circulating water cooling system 100.This zero-emission type follows
Ring water cooling system 100 includes interior circulation cooling system 110 and external circulation cooling system 120.The work of interior circulation cooling system 110
Making medium is cooling water, and the working media of external circulation cooling system 120 is cold-producing medium.External circulation cooling system 120 is followed using it
The cooling water of the cold-producing medium inner loop cooling system 110 that ring uses is cooled down, to improve the system of interior circulation cooling system 110
Cold effect.Zero-emission type circulating water cooling system 100 is enclosed system on the whole, generally circulating cooling pattern.Cooling
The recycling of water, not only reduces the consumption of raw water, saving water resource with operating cost it is thus also avoided that the discharge of cooling water,
The raw water zero achieving zero-emission type circulating water cooling system 100 consumes and wastewater zero discharge, not only economizes on resources and can also prevent
Only pollute.
Further, in the present embodiment, the interior circulation cooling system 110 of zero-emission type circulating water cooling system 100
Cooling water is desalted water.Fouling can be prevented using desalted water, because zero-emission type circulating water cooling system 100 is enclosed
System, therefore the amount of the desalted water in interior circulation cooling system 110 is basically unchanged, interior all can reach prevents fouling for a long time
Purpose, advantageously ensures that the stability of cooling effect of zero-emission type circulating water cooling system 100 the use longevity of extension device
Life.
It should be noted that in other embodiments of the invention, the cooling water of interior circulation cooling system 110 can also be
Other coolants outside desalted water.
Further, in the present embodiment, external circulation cooling system 120 is used for the cooling for interior circulation cooling system 110
Water extraction semen donors.Interior circulation cooling system 110 include circulating water line 111 and be installed on circulating water line 111 for cold
But the first cooler 112 of thermal medium, for cooling down the second cooler 113 of cooling water and be used for driving cooling water in recirculated water
The circulating pump 114 of flowing in pipeline 111.External circulation cooling system 120 includes refrigerant circulation line 121 and is installed on refrigeration
The refrigerant cycle apparatus 122 of agent circulation line 121, refrigerant cooler 123 and decompressor 124.
Interior circulation cooling system 110 and external circulation cooling system 120 all achieve to working media recycle so that
Zero-emission type circulating water cooling system 100 improves it to greatest extent and recycles ability, has reached wastewater zero discharge.Not only
Economize in raw materials, also very friendly to environment.
Further, in the present embodiment, along cooling water in the flow direction of circulating water line 111, with the first cooler 112 it is
Starting point, is followed successively by the first cooler 112, the second cooler 113 and circulating pump 114.
Specifically, in the present embodiment, the cooling water of the coolant outlet of the first cooler 112 and the second cooler 113
Import is connected by circulating water line 111；The coolant outlet of the second cooler 113 and the import of circulating pump 114 are by circulating water pipe
Road 111 connects；The outlet of circulating pump 114 is connected by circulating water line 111 with the cooling water inlet of the first cooler 112.
The cyclic process with the first cooler 112 as starting point for the cooling water is：Cooling water is in the first cooler 112 and thermal medium
Enter the second cooler 113 after carrying out heat exchange to be cooled down, cooling water after cooling is in the Circulation power of circulating pump 114
Promotion under return the first cooler 112 and again participate in heat exchange.
After cooling water provides cold for thermal medium, cool down through the second cooler 113, cooling water can be made to become cold again
Medium be again to provide the cold of abundance it is ensured that the system of interior circulation cooling system 110 through the thermal medium of the first cooler 112
The stability of cold effect.
Further, in the present embodiment, according to cooling water circulating water line 111 flow direction, the second cooler 113
Upstream is additionally provided with air precooler 115.Air precooler 115 is between the first cooler 112 and the second cooler 113.
Specifically, the coolant outlet of the first cooler 112 and the import of air precooler 115 are by circulating water line 111
Connection；The outlet of air precooler 115 is connected by circulating water line 111 with the cooling water inlet of the second cooler 113.
Inventors herein have recognized that：The key factor of the power of decision air precooler 115 is air precooler 115
Outlet temperature and the temperature difference of ambient temperature.The temperature difference reduces, and air precooler 115 power is substantially increased.External circulation cooling system 120
Setting the outlet temperature of air precooler 115 is improved, increase outlet temperature and the environment of air precooler 115
The temperature difference of temperature, reduces the load of air precooler 115, effectively reduces the power consumption of air precooler 115.
It should be noted that in other embodiments of the invention, circulating pump 114 can be installed on the first cooler 112
Coolant outlet at, be also mountable to the exit of air precooler 115.
Further, in the present embodiment, the first cooler 112 is plate-fin heat exchanger.Plate-fin heat exchanger allows many
Stock thermal medium and desalted water heat exchange simultaneously, reduce the quantity of cooler in factory, reduce equipment investment.Additionally, the first cooler
112 adopt plate-fin heat exchanger, also have the advantages that in unit volume, heat exchange area is big, heat exchange efficiency is high, compact conformation.
The present embodiment adopts plate-fin heat exchanger as the first cooler 112, and cooling water is desalted water, there is not fouling
The outlet temperature of risk, therefore cooling water can reach 60 DEG C～80 DEG C, imports and exports the temperature difference up to 30 DEG C～50 DEG C, significantly reduces
The cooling water inflow of circulation, decreases equipment scale and cost of investment.Plus plate-fin heat exchanger, there is heat-transfer surface in unit volume
Long-pending big, heat exchange efficiency is high, compact conformation the advantages of, therefore in the present embodiment, generally, using a platen fin heat exchanger
Can ensure that heat exchange is normally carried out as the first cooler 112, cooler quantity in factory is so greatly reduced, reduce
Equipment investment.
Further, in the present embodiment, refrigerant cycle apparatus 122 include compressor 122a.
Further, the second cooler 113 is heat exchanger, and the second cooler 113 has the cooling passed through for cooling water
Water lines and the refrigerant line passing through for cold-producing medium, that is, in the second cooler 113, cold-producing medium provides cold for cooling water
Amount completes the cooling to cooling water.Interior circulation cooling system 110 and external circulation cooling system 120 using the second cooler 113 as
Joint.
Specifically, the refrigerant outlet of the second cooler 113 and the import of compressor 122a are by refrigerant circulation line 121
Connection, the outlet of compressor 122a is connected by refrigerant circulation line 121 with the import of refrigerant cooler 123.Cold-producing medium is cold
But between the outlet of device 123 and the refrigerant inlet of the second cooler 113, decompressor 124, the going out of refrigerant cooler 123 are set
Mouth is connected by refrigerant circulation line 121 with the import of decompressor 124, the system exporting with the second cooler 113 of decompressor 124
Cryogen import is connected by refrigerant circulation line 121.
Further, in the present embodiment, cold-producing medium be ammonia, nitrogen, methane, ethane, ethylene, propane, propylene, butane,
Any one in pentane and freon.
The cyclic process with the second cooler 113 as starting point for the cold-producing medium is：Gaseous refrigerant is by the system of the second cooler 113
Cryogen outlet is flowed out, and enters refrigerant cooler 123 and is condensed into liquid phase, liquid phase refrigerant is through subtracting after entering compressor 122a supercharging
Reenter the second cooler 113 after depressor 124 decompression and participate in heat exchange, in the second cooler 113, liquid phase refrigerant absorbs
Heat in cooling water and be gasificated into vapor phase refrigerant, and flow out from the refrigerant outlet of the second cooler 113, complete refrigeration and follow
Ring.
Due to the further cooling effect of the cooling water of external circulation cooling system 120 inner loop cooling system 110, improve
Second cooler 113 is to the cooling effect of cooling water so that cooling number is can fully be cooled down it is ensured that by circulating pump
The cooling waters of 114 return the first coolers 112 can provide sufficient cold for thermal medium it is ensured that thermal medium obtain sufficiently cold
But, further increase the cooling of the cooling effect to thermal medium for the interior circulation cooling system 110 and interior circulation cooling system 110
The stability of effect.The overall cooling effect of zero-emission type circulating water cooling system 100 is stable, the sustainable cold providing abundance,
Will not be occurred due to the prolongation of cool time cooling water mean temperature raise situation it is ensured that cooling stability.
Inventors herein have recognized that：When the cooling water temperature of the import of air precooler 115 is of about 40 DEG C, by carrying
The outlet temperature of high air precooler 115 and make the inlet temperature of air precooler 115 and the temperature difference of outlet temperature by 10 DEG C
When being reduced to 5 DEG C, the power consumption incrementss of external circulation cooling system 120 are significantly less than the power consumption decrement of air precooler 115, that is,
Total power consumption of zero-emission type circulating water cooling system 100 has obvious reduction.Particularly when air precooler 115 outlet temperature with
When the ambient temperature temperature difference is less, the power of air precooler 115 sharply increases, and the application passes through setting the second cooler 113 can
To improve the outlet temperature of air precooler 115, to reduce the unnecessary waste of energy of air precooler 115, drop simultaneously
Low power consumption.The power consumption of zero-emission type circulating water cooling system 100 has obtained abundant reduction, has saved operating cost.
In the present embodiment, use high temperature section cooling, such as more than 35 DEG C of warm area, using air precooler 115
Cooling is larger with the temperature difference of ambient temperature due to outlet temperature, and under identical cooling load, the power consumption of air precooler 115 is less than pressure
The cold power consumption of contraction.For the low-temperature zone cooling close with ambient temperature, such as less than 35 DEG C of warm area, due to heat transferring medium temperature
Degree is less with circumstance of temperature difference, and under identical cooling load, air precooler 115 power consumption is much larger than the power consumption of compression refrigeration.
The cooling scheme that embodiments of the invention provide is that air precooler 115, the second cooler 113 and outer circulation are cold
But the comprehensive refrigeration system of system 120, provides high temperature section refrigeration using air precooler 115, and external circulation cooling system 120 provides
Low-temperature zone is freezed, both combinations, reduces the overall power consumption of zero-emission type circulating water cooling system 100 to the full extent.Significantly
Reduce the power consumption cost of refrigeration.
It should be noted that in other embodiments of the invention, refrigerant cycle apparatus 122 can also be by multiple pressures
Contracting machine 122a parallel combination forms.
Existing refrigeration system is all generally used for preparation and is less than 0 DEG C, or even less than -10 DEG C of low temperature, and the present embodiment
The problem faced by zero-emission type circulating water cooling system 100 providing is to need to prepare 20～40 DEG C of high-temperature region.I.e. interior circulation
Cooling system 110 is directly used in the high-temperature region of 20～40 DEG C of preparation, and external circulation cooling system 120 is used for cooling down interior circulation cooling system
The cooling water of system 110.
Generally, the cryogenic temperature of external circulation cooling system 120 is 0 DEG C～40 DEG C, belongs to high-temperature region refrigeration, and low
Warm area refrigeration is compared, high cooling efficiency, and condensation temperature is also of a relatively high, and external circulation cooling system 120 energy-saving benefit is good.Additionally,
For interior circulation cooling system 110, interior circulation cooling system 110 is used for the high-temperature region of 20～40 DEG C of preparation, and cooling water exists
The outlet temperature of air precooler 115 is of a relatively high, and the condensation temperature of external circulation cooling system 120 is of a relatively high, energy-saving benefit
Preferably.
The operation principle of zero-emission type circulating water cooling system 100 is：After cooling water provides cold for thermal medium, through sky
Gas precooler 115 and the dual-cooled of the second cooler 113, make cooling water again can provide sufficient cold for thermal medium.
Particularly external circulation cooling system 120 to the cooling effect again of cooling water so that cooling water is sufficiently cool and obtain enough cold
Amount, makes cooling water can provide sufficient cold for thermal medium, improves the cooling effect of interior circulation cooling system 110.
Zero-emission type circulating water cooling system 100 generally circulating cooling pattern, circulating water uses, and greatly reduces
The consumption of cooling water, saving water resource and operating cost.Cooling water is recycled due to repeatable, and no waste water produces, Ke Yida
To wastewater zero discharge, prevent the pollution of the environment.The zero-emission type circulating water cooling system 100 being provided using the present embodiment, can be significantly
Reduce cooling water amount, and can reach wastewater zero discharge, prevent from polluting, make water-deficient area and the high area of environmental requirement
Plant condition can be met.
Embodiment 2
Refer to Fig. 2, a kind of zero-emission type circulating water cooling system 200 that the present embodiment provides.Zero-emission type recirculated water
What cooling system 200 was different with zero-emission type circulating water cooling system 100 is：Zero-emission type circulating water cooling system 200
External circulation cooling system 220 also include extender cycling element 222；The working media of extender cycling element 222 is to expand
Agent.
Further, in the present embodiment, extender cycling element 222 includes decompressor 222a, extender cooler
222b, booster pump 222c and the vaporizer 222d carrying out heat exchange for extender and thermal medium.The outlet of decompressor 222a with
The inlet communication of extender cooler 222b, the outlet of extender cooler 222b and the extender entrance of vaporizer 222d are by increasing
Press pump 222c connects, and the extender of vaporizer 222d exports the inlet communication with decompressor 222a.The power of decompressor 222a is defeated
Go out portion to be connected with the compression power input unit of compressor 122a.
Further, extender can be ammonia, nitrogen, methane, ethane, ethylene, propane, propylene, butane, pentane and fluorine profit
Any one in high, in the present embodiment, the extender of extender cycling element 222 is propane.
Further, in the present embodiment, the power output shaft of decompressor 222a is defeated with the compression power of compressor 122a
Enter axle coaxially connected.
The cyclic process with booster pump 222c as starting point for the extender is：Liquid phase extender intensified pump 222c supercharging is laggard
Enter vaporizer 222d, extender is converted into high pressure vapor after vaporizer 222d absorbs the heat of thermal medium, enters back into expansion
Machine 222a carries out expansion work, temperature drop and reduced pressure after extender expansion work, and it is cold that subsequent extender enters extender
But device 222b is condensed into liquid phase state, and liquid phase extender enters booster pump 222c again carries out supercharging becomes high-pressure liquid phase expansion
Agent, and then Returning evaporimeter 222d carries out heat exchange with thermal medium.
When extender expands in decompressor 222a and externally does work, the power that its work done passes through decompressor 222a is defeated
Go out portion to conduct to the compression power input unit of compressor 122a, provide power for compressor 122a, define " expansion-compression "
Complementary energy saver mode, reduces the power consumption of compressor 122a to a certain extent, has saved the energy and operating cost.
In vaporizer 222d, extender can absorb heat, provides cold for thermal medium, vaporizer 222d can be used for cold
But thermal medium or absorption industrial waste heat, not only fully serve refrigeration endothermic effect, also make whole zero-emission type circulating water
System 200 can realize the supplement of the energy consumption of the compressor 122a to itself using industrial heat, takes full advantage of industry surplus
Complementary energy source, substantially increases the utilization rate of the energy, cost-effective.Further, since vaporizer 222d can be used for absorbing heat Jie
The heat of matter, and for thermal medium provide cold, therefore zero-emission type circulating water cooling system 200 have more preferable cooling effect and
Energy utilization rate is higher, more energy-conservation.
It should be noted that in other embodiments of the invention, the first cooler 112 can also be arranged in parallel by multiple
Shell-and-tube heat exchanger substitute, as shown in Figure 3.In actual application, for super-huge device, due to plant area relatively
Greatly, each heat exchange unit is apart from each other, if whole thermal mediums are all introduced in plate-fin heat exchanger, the runner mistake of each thermal medium
Long, resistance drop is excessive, so carrying out cooling down advantageously with shell-and-tube heat exchanger respectively.
The operation principle of zero-emission type circulating water cooling system 200 is：By arranging the complementary energy-conservation mould of " expansion-compression "
Formula, the extender of extender cycling element 222 absorbs thermal medium heat or industrial waste heat in vaporizer 222d, is then expanding
Machine 222a expansion work, provides power for compressor 122a, not only reduces the cooling load of interior circulation cooling system 110, subtracts
Lack the consumption of cooling water, decreased equipment size and investment, and also reduced the power consumption of compressor 122a, save operation
Cost.The zero-emission type circulating water cooling system 200 being provided using embodiment, can greatly reduce cooling water water consumption, and can
Reach wastewater zero discharge, prevent from polluting, make water-deficient area and the high area of environmental requirement also can meet plant condition.
Embodiment 3
Refer to Fig. 4, the present embodiment provides a kind of zero-emission type circulating water cooling system 300, zero-emission type recirculated water cooling
But system 300 and the different part of zero-emission type circulating water cooling system 100 are：Zero-emission type circulating water cooling system
300 external circulation cooling system 320 also includes extender cycling element 322, and the working media of extender cycling element 322 is swollen
Swollen dose.
Further, extender cycling element 322 is included decompressor 322a, booster pump 322b and is situated between with heat for extender
Matter carries out the vaporizer 322c of heat exchange.The outlet of decompressor 322a and the inlet communication of refrigerant cooler 123, vaporizer
The extender import of 322c is connected by booster pump 322b with the outlet of refrigerant cooler 123, and the extender of vaporizer 322c goes out
Mouthful with the inlet communication of decompressor 322a；The power output portion of decompressor 322a is connected with the compression power input unit of compressor 122a
Connect.
It should be noted that extender and cold-producing medium be same medium and can be ammonia, nitrogen, methane, ethane, ethylene,
Any one in propane, propylene, butane, pentane and freon.In the present embodiment, medium is ammonia.
The cyclic process that medium is exported as starting point with refrigerant cooler 123 is：Outlet by refrigerant cooler 123
The medium of the liquid phase flowing out is split into two strands, and one medium enters vaporizer 322c after entering booster pump 322b supercharging and absorbs heat
The heat of medium or industrial waste heat become high pressure vapor, and this strand of medium subsequently enters decompressor 322a expansion work, media expansion
Work is sent to the compression power input unit of compressor 122a by the power output portion of decompressor 322a, and this strand of medium is expanding
It is changed into low-pressure vapor phase after acting, return to refrigerant cooler 123 and again cool down and be condensed into liquid phase；Another strand of medium is through decompression
After device 124 decompression, enter the second cooler 113, absorb the heat of cooling water in the second cooler 113, gasify as low-pressure vapor phase
Medium, after the medium that the refrigerant outlet of the second cooler 113 flows out enters and is pressurized compressor 122a, enter cold-producing medium
Again it is condensed into liquid phase in cooler 123
In the present embodiment, extender and cold-producing medium are same medium, in the base of zero-emission type circulating water cooling system 200
On plinth, zero-emission type circulating water cooling system 300 enormously simplify external circulation cooling system 320 it is not necessary to circulate extender
Unit 322 is separately provided, and reduces equipment investment cost and amasss with outfit of equipment, and decreases chemical substance group in system simultaneously
Dosis refracta is so that system operation is more stable, safety.Additionally, the medium of outlet outflow of compressor 122a and decompressor 322a
The medium temperature that flows out of outlet all relatively low but the two temperature is not necessarily identical, enter back into refrigerant cooler after the two mixing
123 are disposably cooled down, and can avoid arranging two refrigerant cooler 123, and refrigerant cooler 123 only need to be to mixing
Ammonia afterwards carries out a cooling treatment, and cooling range is relatively fixing, and the equipment of not only simplify reduces operating cost, and makes
The refrigeration temperature difference of refrigerant cooler 123 is substantially constant, reduces power consumption.
Further, in the present embodiment, it is provided between vaporizer 322c and the first cooler 112 and pass through for thermal medium
Arm 324, arm 324 connects the thermal medium inlet of thermal medium outlet and first cooler 112 of vaporizer 322c.
In actual applications, as needed, can select to make all or part of thermal medium pass sequentially through vaporizer 322c, prop up
Pipe 324 and the first cooler 112, are cooled down respectively in vaporizer 322c with the first cooler 112 twice, improve to whole
Or the cooling effect of part thermal medium.When not needing to be cooled down twice, thermal medium can only be entered by the first cooler 112
Row cooling, and now vaporizer 322c can be used for absorbing industrial waste heat, prevents used heat from polluting.
The operation principle of zero-emission type circulating water cooling system 300 is：By extender and cold-producing medium are used same Jie
Matter replaces, and makes compression process and expansion process be in same circulation, compared with zero-emission type circulating water cooling system 200,
Enormously simplify device structure, reduce equipment investment cost, and because medium only need to be carried out once in refrigerant cooler 123
Property cool, simplify the cooling procedure of medium, decrease power consumption, energy saving, and cooling water is due to repeatable circulation
Use, wastewater zero discharge can be reached, prevent the pollution of the environment.
Embodiment 4
Refer to Fig. 5, the present embodiment provides a kind of zero-emission type circulating water cooling system 400.Zero-emission type recirculated water cooling
But system 400 is compared with zero-emission type circulating water cooling system 100, except for the difference that：Zero-emission type circulating water cooling system 400
The refrigerant cycle apparatus 422 of external circulation cooling system 420 include absorber 422a, solution pump 422b and for entering with thermal medium
The generator 422c of row heat exchange, the cold-producing medium of external circulation cooling system 420 is absorbing liquid and combining of circulating agent.
Specifically, the circulation agent inlet communication of the refrigerant outlet of the second cooler 113 and absorber 422a, absorber
The outlet of 422a is connected by solution pump 422b with the import of generator 422c, and the circulation agent outlet of generator 422c is cold with cold-producing medium
But the refrigerant inlet connection of device 123, the absorbing liquid outlet of generator 422c and the absorbing liquid inlet communication of absorber 422a.
Further, absorbing liquid is water and circulates agent for ammonia；Or absorbing liquid is lithium bromide and circulates agent for water.
Circulation agent enters absorber 422a after the second cooler 113 endothermic gasification, goes out from the absorbing liquid of generator 422c
The absorbing liquid import through absorber 422a for the absorbing liquid (lean solution) that mouth flows out enters absorber 422a and gaseous circulation agent is carried out
Absorb, the absorbing liquid absorbing circulation agent becomes rich solution, after solution pump 422b supercharging, enter generator 422c.
After rich solution carries out heat exchange with thermal medium in generator 422c, can be by circulation agent therein again with gaseous shape
Formula discharges, and gaseous recycle agent enters refrigerant cooler 123 condensation liquefaction, liquefaction by the circulation agent outlet of generator 422c
Circulation agent afterwards enters the second cooler 113 and again provides cold for thermal medium after being reduced pressure by decompressor 124.Meanwhile, exist
The absorbing liquid releasing circulation agent in generator 422c enters absorber 422a absorption gaseous recycle agent again, so completes to follow
Ring.
Further, in the present embodiment, with zero-emission type circulating water cooling system 100, zero-emission type circulating water
Unlike system 200 and zero-emission type circulating water cooling system 300, zero-emission type circulating water cooling system 400 need not be pressed
Contracting machine 122a, decompressor 222a etc., reduce power consumption, also improve stability simultaneously, further simplified device structure, subtract
Little equipment volume and equipment investment cost.Meanwhile, zero-emission type circulating water cooling system 400 equally can be with Selection utilization
Two coolers 113 and generator 422c carry out dual-cooled to thermal medium, improve cooling effect.
The operation principle of zero-emission type circulating water cooling system 400 is：By absorbing liquid to the absorption circulating agent and release
Realize the cooling of thermal medium and external circulation cooling system 420 are recycled to cold-producing medium, reduce power consumption simplifying and set
It is achieved that zero-emission while standby.Additionally, cooling effect and cooling stability are also guaranteed and improve.And cooling water
Recycled due to repeatable, wastewater zero discharge can be reached, prevent the pollution of the environment.
In sum, the zero-emission type circulating water cooling system 100 of present invention offer, zero-emission type circulating water cooling system
200th, zero-emission type circulating water cooling system 300 and zero-emission type circulating water cooling system 400 are respectively provided with good cooling results, electricity
Consume low, the low advantage of operating cost, and due to zero-emission type circulating water cooling system 100, zero-emission type circulating water system
System 200, zero-emission type circulating water cooling system 300 and zero-emission type circulating water cooling system 400 are enclosed circulation
Cooling system, can also greatly reduce cooling water or the consumption of other cold-producing mediums and cooling water, not only cost-effective and also can
Substantially to realize zero-emission, environmental friendliness.Further, since each zero system generally circulating cooling above, circulating water makes
With greatly reducing the consumption of cooling water, saving water resource and operating cost.Cooling water is recycled due to repeatable, permissible
Reach zero-emission, prevent the pollution of the environment.Using system above, cooling water water consumption can be greatly reduced, so that water-deficient area also can be expired
Sufficient plant condition.
The foregoing is only the preferred embodiments of the present invention, be not limited to the present invention, for the skill of this area
For art personnel, the present invention can have various modifications and variations.All within the spirit and principles in the present invention, made any repair
Change, equivalent, improvement etc., should be included within the scope of the present invention.
Claims (10)
1. a kind of zero-emission type circulating water cooling system is it is characterised in that in described zero-emission type circulating water cooling system includes
Circulating cooling system and the external circulation cooling system for providing cold for described interior circulation cooling system；
The working media of described interior circulation cooling system be cooling water, described interior circulation cooling system include circulating water line and
It is installed on the first cooler for cooling down thermal medium, second cooling for cooling down described cooling water of described circulating water line
Device and the circulating pump for driving described cooling water to flow in described circulating water line；
The working media of described external circulation cooling system is cold-producing medium, and described external circulation cooling system includes refrigerant circulation line
And it is installed on refrigerant cycle apparatus, refrigerant cooler and the decompressor of described refrigerant circulation line.
2. zero-emission type circulating water cooling system according to claim 1 is it is characterised in that according to described cooling water in institute
State the flow direction of circulating water line, the upstream of described second cooler is additionally provided with air precooler.
3. zero-emission type circulating water cooling system according to claim 1 is it is characterised in that described refrigerant cycle apparatus
Including compressor, the refrigerant outlet of described second cooler and the inlet communication of described compressor, the outlet of described compressor
Inlet communication with described refrigerant cooler.
4. zero-emission type circulating water cooling system according to claim 3 is it is characterised in that described cold-producing medium is ammonia, nitrogen
Any one in gas, methane, ethane, ethylene, propane, propylene, butane, pentane and freon.
5. zero-emission type circulating water cooling system according to claim 1 is it is characterised in that described refrigerant cycle apparatus
Including absorber, solution pump and the generator for carrying out heat exchange with thermal medium, described cold-producing medium is absorbing liquid and circulation agent
Combination；
The circulation agent inlet communication of the refrigerant outlet of described second cooler and described absorber, the outlet of described absorber with
The import of described generator is connected by described solution pump, the circulation agent outlet of described generator and the entering of described refrigerant cooler
Mouth connection, the absorbing liquid outlet of described generator and the absorbing liquid inlet communication of described absorber.
6. zero-emission type circulating water cooling system according to claim 5 is it is characterised in that described absorbing liquid is water and institute
Stating circulation agent is ammonia；Or for lithium bromide and described circulation agent is water to described absorbing liquid.
7. zero-emission type circulating water cooling system according to claim 3 is it is characterised in that described external circulation cooling system
Also include extender cycling element；The working media of described extender cycling element is extender；Described extender cycling element
Including decompressor, extender cooler, booster pump and the vaporizer carrying out heat exchange for extender and thermal medium, described expansion
The outlet of machine and the inlet communication of described extender cooler, the outlet of described extender cooler and the expansion of described vaporizer
Agent entrance is connected by described booster pump, and the extender of described vaporizer exports the inlet communication with described decompressor；Described expansion
The power output portion of machine is connected with the compression power input unit of described compressor.
8. zero-emission type circulating water cooling system according to claim 3 is it is characterised in that described external circulation cooling system
Also include extender cycling element；Described extender cycling element includes decompressor, booster pump and is used for extender and thermal medium
Carry out the vaporizer of heat exchange；The outlet of described decompressor and the inlet communication of described refrigerant cooler, described vaporizer
Extender import is connected by described booster pump with the outlet of described refrigerant cooler, and the extender of described vaporizer exports and institute
State expander inlet connection；The power output portion of described decompressor is connected with the compression power input unit of described compressor.
9. the zero-emission type circulating water cooling system according to claim 7 or 8 is it is characterised in that described vaporizer and institute
State and between the first cooler, be provided with the arm passing through for thermal medium, described arm connect the thermal medium outlet of described vaporizer with
The thermal medium inlet of described first cooler.
10. zero-emission type circulating water cooling system according to claim 1 is it is characterised in that described first cooler is
Plate-fin heat exchanger.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611036409.4A CN106403453A (en) | 2016-11-21 | 2016-11-21 | Zero discharge type circulating water cooling system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611036409.4A CN106403453A (en) | 2016-11-21 | 2016-11-21 | Zero discharge type circulating water cooling system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106403453A true CN106403453A (en) | 2017-02-15 |
Family
ID=58082427
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201611036409.4A Pending CN106403453A (en) | 2016-11-21 | 2016-11-21 | Zero discharge type circulating water cooling system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106403453A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107388693A (en) * | 2017-07-31 | 2017-11-24 | 河南开元空分集团有限公司 | A kind of novel energy-conserving closed circle water system |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101344345A (en) * | 2008-08-14 | 2009-01-14 | 安徽工业大学 | Compression-absorption-diffusion combined refrigerating plant and its refrigeration cycle method |
| CN103175334A (en) * | 2011-12-23 | 2013-06-26 | 江苏合正能源科技有限公司 | Heat power type industrial refrigeration machine |
| CN103438598A (en) * | 2013-08-20 | 2013-12-11 | 中国科学院工程热物理研究所 | Cascading refrigerating system and method based on forward and reverse cycle coupling |
| US20140338391A1 (en) * | 2013-03-15 | 2014-11-20 | Inertech Ip Llc | Multi-stage evaporative heat rejection process cycle that facilitates process cooling efficiency, water production, and/or water reclamation for fluid coolers and cooling towers |
| CN105910456A (en) * | 2016-06-12 | 2016-08-31 | 北京烨晶科技有限公司 | Green comprehensive cold island equipment and cooling method |
| CN206247730U (en) * | 2016-11-21 | 2017-06-13 | 成都赛普瑞兴科技有限公司 | A kind of zero-emission type circulating water cooling system |
-
2016
- 2016-11-21 CN CN201611036409.4A patent/CN106403453A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101344345A (en) * | 2008-08-14 | 2009-01-14 | 安徽工业大学 | Compression-absorption-diffusion combined refrigerating plant and its refrigeration cycle method |
| CN103175334A (en) * | 2011-12-23 | 2013-06-26 | 江苏合正能源科技有限公司 | Heat power type industrial refrigeration machine |
| US20140338391A1 (en) * | 2013-03-15 | 2014-11-20 | Inertech Ip Llc | Multi-stage evaporative heat rejection process cycle that facilitates process cooling efficiency, water production, and/or water reclamation for fluid coolers and cooling towers |
| CN103438598A (en) * | 2013-08-20 | 2013-12-11 | 中国科学院工程热物理研究所 | Cascading refrigerating system and method based on forward and reverse cycle coupling |
| CN105910456A (en) * | 2016-06-12 | 2016-08-31 | 北京烨晶科技有限公司 | Green comprehensive cold island equipment and cooling method |
| CN206247730U (en) * | 2016-11-21 | 2017-06-13 | 成都赛普瑞兴科技有限公司 | A kind of zero-emission type circulating water cooling system |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107388693A (en) * | 2017-07-31 | 2017-11-24 | 河南开元空分集团有限公司 | A kind of novel energy-conserving closed circle water system |
| CN107388693B (en) * | 2017-07-31 | 2023-11-10 | 河南开元空分集团有限公司 | Energy-saving closed circulating water system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN114198170B (en) | Carbon dioxide energy storage system based on double heat storage loops and working method thereof | |
| CN104913541B (en) | Stirling cycle and the direct-coupled refrigeration machine of Vapor Compression Refrigeration Cycle and method | |
| CN109763948A (en) | A kind of supercritical carbon dioxide solar heat power generation system and operation method | |
| CN109579432B (en) | Natural gas and electric power interconnection peak shaving system utilizing low-temperature liquefaction for energy storage | |
| CN206695421U (en) | LNG cold energy refrigerating circulatory devices | |
| CN203561058U (en) | Hot water unit of carbon dioxide heat pump | |
| CN105066508A (en) | Efficient injection and absorption refrigerator for freezing and refrigeration | |
| CN208704208U (en) | A kind of cascade refrigeration formula high temperature water source heat pump units | |
| CN114198173A (en) | Full-backheating Brayton cycle and absorption refrigeration integrated electricity-cold combined supply system | |
| CN206247730U (en) | A kind of zero-emission type circulating water cooling system | |
| CN106403453A (en) | Zero discharge type circulating water cooling system | |
| CN1137359C (en) | Lithium bromide absorption type refrigerator suitable for large temp differnece and able to fully utilize energy | |
| CN204593940U (en) | A kind of Stirling cycle and the direct-coupled refrigeration machine of Vapor Compression Refrigeration Cycle | |
| CN103090486A (en) | Heat balance all-in-on machine | |
| CN105091401A (en) | Jet absorption refrigerating device with copious cooling effect | |
| CN211777626U (en) | Liquid air energy storage system | |
| CN209539413U (en) | A kind of low parameter heat recovery system | |
| CN202941181U (en) | Warehouse drying air supply treatment grain storage system based on heat recovery technology | |
| CN219559573U (en) | Hot water recycling system for vinyl chloride synthesis reaction | |
| CN111520207A (en) | Supercritical Brayton cycle power generation system and method with flow dividing, throttling and cooling functions | |
| CN111305922A (en) | Liquid air energy storage system | |
| CN218380586U (en) | Liquid hydrogen liquid bath vaporization heat exchange system | |
| CN220959759U (en) | Heat exchange system | |
| CN215809432U (en) | Waste heat recovery utilizes device in concentrated nitric acid production | |
| CN214620169U (en) | Cold and hot water supply system for producing silicon wafers |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20170215 |