CN208108535U - A kind of lithium bromide adsorption water chilling machine set system of band evaporation cooling heat exchange device - Google Patents
A kind of lithium bromide adsorption water chilling machine set system of band evaporation cooling heat exchange device Download PDFInfo
- Publication number
- CN208108535U CN208108535U CN201820437677.5U CN201820437677U CN208108535U CN 208108535 U CN208108535 U CN 208108535U CN 201820437677 U CN201820437677 U CN 201820437677U CN 208108535 U CN208108535 U CN 208108535U
- Authority
- CN
- China
- Prior art keywords
- cooling
- water
- heat exchange
- exchange device
- evaporation
- 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.)
- Active
Links
Classifications
-
- 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
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A30/00—Adapting or protecting infrastructure or their operation
- Y02A30/27—Relating to heating, ventilation or air conditioning [HVAC] technologies
-
- 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]
- Y02B30/62—Absorption based systems
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Abstract
A kind of lithium bromide adsorption water chilling machine set system of band evaporation cooling heat exchange device, belongs to air conditioner technical field.In the water chilling unit system, absorber, regenerator, heat exchanger, weak solution pump, concentrated solution pump group are at lithium-bromide solution cycling element, regenerator or absorber are connected with evaporation cooling heat exchange device, evaporation cooling heat exchange device is made of interior circulation and outer circulation, the recirculated water of outer circulation is not in contact with the refrigerant of interior circulation or cooling water, it is only exchanged heat by evaporating cooling heat exchange device, the heat of solution in regenerator or absorber is cooled down.The utility model replaces the cooling tower in the condenser and traditional lithium bromide adsorption water chilling machine set system of traditional lithium bromide adsorption water chilling unit using evaporation cooling heat exchange device, the cooling water inflow of 30%-45% can be reduced, cooling water drifts loss when greatly reducing the investment cost of cooling tower and cooling water pump and operating power consumption in system, while reducing cooling tower operation.
Description
Technical field
The utility model belongs to air conditioner technical field, and in particular to a kind of lithium bromide of band evaporation cooling heat exchange device
Absorption chiller system.
Background technique
The absorber of traditional lithium bromide adsorption water chilling unit and the type of cooling of condenser mainly use open type cooling
Tower cooling by water, i.e., by the way that recirculated water with spray pattern, on spray to the filler of glass fibre, is passed through connecing for water and air
Touching reaches heat exchange, then drives tower interior air-flow circulation by blower, the thermal current after exchanging heat with water is taken out of, to reach cooling
Purpose.Such type of cooling needs to configure biggish cooling tower, cooling water water pump, has and takes up a large area, initial investment height etc.
Problem, and cooling water flow is big, and cooling water system lift is high, and cooling water water pump conveying energy consumption is higher, in addition open cooling tower
When operation, drift ice phenomenon can be generated, water loss is caused, frequent moisturizing, while can also be polluted to a certain extent cold
But water makes its deteriorating water quality, and extraneous sundries can also enter in cooling water, cause water pollution.
Utility model content
In order to solve the above problem, the utility model provides a kind of lithium bromide adsorption water chilling of band evaporation cooling heat exchange device
Machine set system is cooled down the heat for the refrigerant vapour that solution concentration generates in regenerator by the latent heat of water evaporation, thus
Realize the purpose that traditional lithium bromide adsorption water chilling train condenser is replaced using evaporation cooling heat exchange device；Pass through water evaporation
Latent heat the heat of cooling water in absorber is cooled down, replace traditional bromine using evaporation cooling heat exchange device to realize
Change the purpose of the cooling tower in lithium-absorbing formula water chilling unit system.
The utility model technical solution used for the above purpose is：A kind of bromine of band evaporation cooling heat exchange device
Change lithium-absorbing formula water chilling unit system, absorber is connect with evaporator, and regenerator is connect with refrigerant vapour reservoir, absorber,
Regenerator, heat exchanger, weak solution pump, concentrated solution pump group are at lithium-bromide solution cycling element, it is characterised in that：The regenerator
Or absorber is connected with evaporation cooling heat exchange device, the evaporation cooling heat exchange device is made of interior circulation and outer circulation, is followed outside
The recirculated water of ring is not in contact with the refrigerant of interior circulation or cooling water, is only exchanged heat by evaporating cooling heat exchange device, will
The heat of solution is cooled down in regenerator or absorber.
The regenerator connection evaporation cooling heat exchange device one, evaporation cooling heat exchange device one are sprayed by header tank one, circulation
Shower device one, cooling coil one form, and recirculated water is spread outside the pipe of cooling coil one, manage in cryogen flowing, cooling coil one with
Refrigerant vapour reservoir, cryogen condensate reservoir constitute circulation, header tank one, circulating sprayer one, cooling coil in enclosed
One and water circulating pump one constitute the outer circulation of air and water heat exchange, the recirculated water in header tank one is sent to by water circulating pump one to follow
Ring spray shower device one, then the heat that evaporation on cooling coil one absorbs the refrigerant vapour inside cooling coil one is spread to, most
After return header tank one, the recirculated water of outer circulation is not in contact with the refrigerant of interior circulation, is only carried out by cooling coil one
Heat exchange cools down the heat that solution in regenerator is concentrated.
The regenerator and refrigerant vapour reservoir are arranged in the same cylinder, what the solution concentration in regenerator generated
Refrigerant vapour stores in refrigerant vapour reservoir, passes through refrigerant vapour pipeline between cooling coil one and refrigerant vapour reservoir
Connection is connected between cooling coil one and cryogen condensate reservoir by cryogen condensate line one, in refrigerant vapour reservoir
Refrigerant vapour, which is entered by refrigerant vapour pipeline in the cooling coil one for evaporating cooling heat exchange device one, to be cooled down, after cooling
Water as refrigerant enters cryogen condensate reservoir by cryogen condensate line one, passes through cryogen between cryogen condensate reservoir and evaporator
Condensate line two connects, and water as refrigerant enters evaporator by cryogen condensate line two.
It can be connected to arrangement between the cryogen condensate reservoir and refrigerant vapour reservoir, can also individually be arranged.
Air intlet one is arranged in one top of header tank of the evaporation cooling heat exchange device one, evaporates cooling heat exchange device one
Top be provided with wind exhausting outlet one, be provided at wind exhausting outlet one for the external air draft to evaporation cooling heat exchange device one
Blower one, evaporation cooling heat exchange device one can also be by the way of air-cooled, i.e. evaporation cooling heat exchange device one is by cooling coil
One, blower one forms, no setting is required header tank one, circulating sprayer one and water circulating pump one.
The absorber connection evaporation cooling heat exchange device two, evaporation cooling heat exchange device two are sprayed by header tank two, circulation
Shower device two, cooling coil two form, and recirculated water is spread outside the pipe of cooling coil two, manage in flow of cooling water, absorber and cold
But coil pipe two is constituted in enclosed and is recycled by the cooling water inlet of absorber and the pipeline of cooling water outlet, in cooling coil two
Cooling water is transported to absorber by cooling water circulating pump；Header tank two, circulating sprayer two, cooling coil two and recirculated water
Pump two constitutes the outer loop of air and water heat exchange, and the recirculated water of outer loop is not in contact with the cooling water of interior circulation, only logical
Supercooling coil pipe two exchanges heat, and the heat of cooling water in absorber is cooled down.
Setting evaporation cooling heat exchange device two and cold on the cooling water inlet of the absorber and the pipeline of cooling water outlet
But water-circulating pump, evaporation cooling heat exchange device two connect water circulating pump two.
Air intlet two is arranged in two top of header tank of the evaporation cooling heat exchange device two, evaporates cooling heat exchange device two
Top be provided with wind exhausting outlet two, be provided at wind exhausting outlet two for the external air draft to evaporation cooling heat exchange device two
Blower two, evaporation cooling heat exchange device two can also be by the way of air-cooled, i.e. evaporation cooling heat exchange device two is by cooling coil
Two, blower two forms, no setting is required header tank two, circulating sprayer two and water circulating pump two.
The water chilling unit system is suitable for warm water type, direct combustion type, steam type, flue gas type and compound energy type lithium bromide
Absorption chiller.
The water chilling unit system is suitable for single-effect lithiumbromide absorption chiller and dual effect type suction-type lithium bromide
Water cooler.
The utility model has the beneficial effects that：
1, the refrigerant vapour in the cooling coil of evaporation cooling heat exchange device and cooling are cooled down by the latent heat of water evaporation
The heat of water is replaced the condenser of traditional lithium bromide adsorption water chilling unit using evaporation cooling heat exchange device, can reduce 30%-
45% cooling water inflow is particularly suitable for area and place that water source lacks, and greatly reduces cooling tower and cooling in system
The investment cost of water pump and operating power consumption, while cooling water drifts loss when reducing cooling tower operation；
2, the cooling tower in traditional lithium bromide adsorption water chilling machine set system is replaced using evaporation cooling heat exchange device, absorbed
The cooling water pipeline system of device is closed cycle, and for cooling water almost without the consumption of water, cooling water uses distilled water, and pipeline is not easy
Fouling does not pollute, does not corrode, and can increase the service life of pipeline and equipment；
3, the use for evaporating cooling heat exchange device, eliminates the cooling between lithium bromide adsorption water chilling unit and cooling tower
Water pump greatly reduces the investment cost and operating of cooling tower and cooling water pump in system using lesser cooling water circulating pump
Power consumption；
4, evaporation cooling heat exchange device 16 is installed simply, without excavating underground tank, since cooling water is closed cycle, and pipe
It damages small, needs the caliber of pipeline is opposite to reduce；
5, water phenomenon of floaing is reduced, and the water rate of floaing of open cooling tower is 0.5% or so, evaporates the water rate of floaing of cooling heat exchange device
0.05% can be dropped to, recirculated water drifts loss when reducing cooling tower operation.
Detailed description of the invention
Fig. 1 is traditional lithium bromide adsorption water chilling set structure schematic diagram；
Fig. 2 is that a kind of lithium bromide adsorption water chilling machine set system structure of band evaporation cooling heat exchange device of the utility model is shown
It is intended to；
In figure：1- absorber, 2- evaporator, 3- regenerator, 4- heat exchanger, 5- weak solution pump, 6- concentrated solution pump, 7- are cold
Agent pump, 8- refrigerant vapour reservoir, 9- cryogen condensate reservoir, 10- evaporate cooling heat exchange device one, 11- header tank one, 12-
Water circulating pump one, 13- circulating sprayer one, 14- cooling coil one, 15- blower one, 16- evaporate cooling heat exchange device two,
17- header tank two, 18- water circulating pump two, 19- circulating sprayer two, 20- cooling coil two, 21- blower two, 22- cooling water
Circulating pump, the cooling water inlet A-, B- cooling water outlet, C- cold water inlet, D- cooling water outlet, E- heat source water inlet, F- heat source water
Outlet, G- air intlet one, H- wind exhausting outlet one, I- refrigerant vapour pipeline, J- cryogen condensate line one, K- cryogen condensate line
Two, L- air intlet two, M- wind exhausting outlet two.
Specific embodiment
The present invention will be further described with specific embodiment with reference to the accompanying drawing, but the utility model is not limited to have
Body embodiment.
Embodiment 1
A kind of lithium bromide adsorption water chilling machine set system of band evaporation cooling heat exchange device as shown in Figure 2, absorber 1 with
Evaporator 2 connects, and regenerator 3 connect with refrigerant vapour reservoir 8, absorber 1, regenerator 3, heat exchanger 4, weak solution pump 5,
6 composition lithium-bromide solution cycling element of concentrated solution pump, the regenerator 3 are connected with evaporation cooling heat exchange device with absorber 1,
The evaporation cooling heat exchange device is made of interior circulation and outer circulation, the recirculated water of outer circulation not with the refrigerant of interior circulation or cold
But water phase contacts, and is only exchanged heat by evaporating cooling heat exchange device, the heat of solution in regenerator 3, absorber 1 is carried out cold
But.
The regenerator 3 connection evaporation cooling heat exchange device 1, evaporation cooling heat exchange device 1 by header tank 1,
Circulating sprayer 1, cooling coil 1 form, and recirculated water is spread outside the pipe of cooling coil 1, manage interior cryogen flowing,
Cooling coil 1 and refrigerant vapour reservoir 8, cryogen condensate reservoir 9 constitute circulation in enclosed, header tank 1, circulation spray
Shower device 1, cooling coil 1 and water circulating pump 1 constitute the outer circulation of air and water heat exchange, in header tank 1
Recirculated water is sent to circulating sprayer 1 by water circulating pump 1, then spreads to evaporation on cooling coil 1 and absorb cooling
The heat of refrigerant vapour inside coil pipe 1, finally returns header tank 1, the recirculated water of outer circulation not with interior circulation
Refrigerant be in contact, only exchanged heat by cooling coil 1, the heat that solution in regenerator 3 is concentrated cooled down.
The regenerator 3 is arranged in the same cylinder with refrigerant vapour reservoir 8, and the solution in regenerator 3, which is concentrated, to be produced
Raw refrigerant vapour stores in refrigerant vapour reservoir 8, passes through cryogen between cooling coil 1 and refrigerant vapour reservoir 8
Steam pipework I connection, by the one J connection of cryogen condensate line between cooling coil 1 and cryogen condensate reservoir 9, cryogen steams
Refrigerant vapour in vapour reservoir 8 enters the cooling coil 1 of evaporation cooling heat exchange device 1 by refrigerant vapour pipeline I
In cooled down, water as refrigerant after cooling enters cryogen condensate reservoir 9 by one J of cryogen condensate line, the storage of cryogen condensate
By the two K connection of cryogen condensate line between device 9 and evaporator 2, water as refrigerant enters evaporator 2 by two K of cryogen condensate line.
Arrangement is connected between the cryogen condensate reservoir 9 and refrigerant vapour reservoir 8.
One G of air intlet is arranged in one 11 top of header tank of the evaporation cooling heat exchange device 1, evaporates cooling heat transferring
The top of device 1 is provided with one H of wind exhausting outlet, be provided at one H of wind exhausting outlet for evaporation cooling heat exchange device 1
External air draft blower 1, evaporation cooling heat exchange device 1 can also using air-cooled by the way of, that is, evaporate cooling heat transferring
Device 1 is made of cooling coil 1, blower 1, no setting is required header tank 1, circulating sprayer 1 and circulation
Water pump 1.
The absorber 1 connection evaporation cooling heat exchange device 2 16, evaporation cooling heat exchange device 2 16 by header tank 2 17,
Circulating sprayer 2 19, cooling coil 2 20 form, and recirculated water is spread outside the pipe of cooling coil 2 20, manage interior cooling water flow
Dynamic, absorber 1 and cooling coil 2 20 are made up of in enclosed the pipeline of the cooling water inlet A and cooling water outlet B of absorber 1
It recycles, the cooling water in cooling coil 2 20 is transported to absorber 1 by cooling water circulating pump 22；Header tank 2 17, circulation spray
Shower device 2 19, cooling coil 2 20 and water circulating pump 2 18 constitute the outer loop of air and water heat exchange, and outer loop is followed
Ring water is not in contact with the cooling water of interior circulation, is only exchanged heat by cooling coil 2 20, by the heat of cooling water in absorber 1
Amount is cooled down.
Setting evaporation cooling heat exchange device 2 16 on the pipeline of the cooling water inlet A and cooling water outlet B of the absorber 1
With cooling water circulating pump 22, evaporates cooling heat exchange device 2 16 and connect water circulating pump 2 18.
Two L of air intlet is arranged in 2 17 top of header tank of the evaporation cooling heat exchange device 2 16, evaporates cooling heat transferring
The top of device 2 16 is provided with two M of wind exhausting outlet, be provided at two M of wind exhausting outlet for evaporation cooling heat exchange device 2 16
External air draft blower 2 21, evaporation cooling heat exchange device 2 16 can also using air-cooled by the way of, that is, evaporate cooling heat transferring
Device 2 16 is made of cooling coil 2 20, blower 2 21, no setting is required header tank 2 17, circulating sprayer 2 19 and circulation
Water pump 2 18.
The water chilling unit system is suitable for warm water type, direct combustion type, steam type, flue gas type and compound energy type lithium bromide
Absorption chiller.
The water chilling unit system is suitable for single-effect lithiumbromide absorption chiller and dual effect type suction-type lithium bromide
Water cooler.
Embodiment 2
A kind of lithium bromide adsorption water chilling machine set system of the evaporation cooling heat exchange device of band described in the present embodiment it is each
Part-structure is in the same manner as in Example 1, and difference is：
Only absorber 1 is connected with evaporation cooling heat exchange device, i.e., is connected with evaporation cooling heat exchange device 16, the evaporation
Each section connection of cooling heat exchange device 16 is in the same manner as in Example 1.
Embodiment 3
A kind of lithium bromide adsorption water chilling machine set system of the evaporation cooling heat exchange device of band described in the present embodiment it is each
Part-structure is in the same manner as in Example 1, and difference is：
1）Only regenerator 3 is connected with evaporation cooling heat exchange device, i.e., is connected with evaporation cooling heat exchange device 10, the steaming
Each section connection for sending out cooling heat exchange device 10 is in the same manner as in Example 1；
2）The cryogen condensate reservoir 9 is individually to arrange with refrigerant vapour reservoir 8.
Claims (10)
1. a kind of lithium bromide adsorption water chilling machine set system of band evaporation cooling heat exchange device, absorber（1）With evaporator（2）Even
It connects, regenerator（3）With refrigerant vapour reservoir（8）Connection, absorber（1）, regenerator（3）, heat exchanger（4）, weak solution pump
（5）, concentrated solution pump（6）Form lithium-bromide solution cycling element, it is characterised in that：The regenerator（3）Or absorber（1）With steaming
It sends out cooling heat exchange device to be connected, the evaporation cooling heat exchange device is made of interior circulation and outer circulation, and the recirculated water of outer circulation is not
It is in contact, is only exchanged heat by evaporating cooling heat exchange device, by regenerator with the refrigerant of interior circulation or cooling water（3）Or it inhales
Receive device（1）The heat of middle solution is cooled down.
2. a kind of lithium bromide adsorption water chilling machine set system of band evaporation cooling heat exchange device according to claim 1,
It is characterized in that：The regenerator（3）Connection evaporation cooling heat exchange device one（10）, evaporate cooling heat exchange device one（10）By catchmenting
Case one（11）, circulating sprayer one（13）, cooling coil one（14）Composition, cooling coil one（14）Pipe outside spread circulation
Water manages interior cryogen flowing, cooling coil one（14）With refrigerant vapour reservoir（8）, cryogen condensate reservoir（9）It constitutes in enclosed
Circulation, header tank one（11）, circulating sprayer one（13）, cooling coil one（14）With water circulating pump one（12）Constitute air with
The outer circulation of water heat exchange, header tank one（11）In recirculated water pass through water circulating pump one（12）It is sent to circulating sprayer one
（13）, then spread to cooling coil one（14）Upper evaporation absorbs cooling coil one（14）The heat of internal refrigerant vapour, most
After return header tank one（11）, the recirculated water of outer circulation is not in contact with the refrigerant of interior circulation, only by cooling coil one
（14）It exchanges heat, by regenerator（3）The heat of middle solution concentration is cooled down.
3. a kind of lithium bromide adsorption water chilling machine set system of band evaporation cooling heat exchange device according to claim 2,
It is characterized in that：The regenerator（3）With refrigerant vapour reservoir（8）It is arranged in the same cylinder, regenerator（3）In solution
The refrigerant vapour generated is concentrated in refrigerant vapour reservoir（8）Middle storage, cooling coil one（14）With refrigerant vapour reservoir（8）
Between pass through refrigerant vapour pipeline（I）Connection, cooling coil one（14）With cryogen condensate reservoir（9）Between pass through cryogen condensate
Pipeline one（J）Connection, refrigerant vapour reservoir（8）In refrigerant vapour pass through refrigerant vapour pipeline（I）It is changed into evaporation cooling
Thermal one（10）Cooling coil one（14）In cooled down, water as refrigerant after cooling pass through cryogen condensate line one（J）Into
Enter cryogen condensate reservoir（9）, cryogen condensate reservoir（9）With evaporator（2）Between pass through cryogen condensate line two（K）Even
It connects, water as refrigerant passes through cryogen condensate line two（K）Into evaporator（2）.
4. a kind of lithium bromide adsorption water chilling machine set system of band evaporation cooling heat exchange device according to claim 2,
It is characterized in that：The cryogen condensate reservoir（9）With refrigerant vapour reservoir（8）Between can be connected to arrangement, can also be independent
Arrangement.
5. a kind of lithium bromide adsorption water chilling machine set system of band evaporation cooling heat exchange device according to claim 2,
It is characterized in that：The evaporation cooling heat exchange device one（10）Header tank one（11）Air intlet one is arranged in top（G）, evaporate cold
But heat-exchanger rig one（10）Top be provided with wind exhausting outlet one（H）, wind exhausting outlet one（H）Place is provided with for cooling down to evaporation
Heat-exchanger rig one（10）External air draft blower one（15）, evaporate cooling heat exchange device one（10）Air-cooled side can also be used
Formula, i.e. evaporation cooling heat exchange device one（10）By cooling coil one（14）, blower one（15）Composition, no setting is required header tank one
（11）, circulating sprayer one（13）And water circulating pump one（12）.
6. a kind of lithium bromide adsorption water chilling machine set system of band evaporation cooling heat exchange device according to claim 1,
It is characterized in that：The absorber（1）Connection evaporation cooling heat exchange device two（16）, evaporate cooling heat exchange device two（16）By catchmenting
Case two（17）, circulating sprayer two（19）, cooling coil two（20）Composition, cooling coil two（20）Pipe outside spread circulation
Water manages interior flow of cooling water, absorber（1）With cooling coil two（20）Pass through absorber（1）Cooling water inlet（A）And cooling
Water out（B）Pipeline constitute enclosed in circulation, cooling coil two（20）In cooling water pass through cooling water circulating pump（22）It is defeated
It is sent to absorber（1）；Header tank two（17）, circulating sprayer two（19）, cooling coil two（20）With water circulating pump two（18）
The outer loop of air and water heat exchange is constituted, the recirculated water of outer loop is not in contact with the cooling water of interior circulation, only by cold
But coil pipe two（20）It exchanges heat, by absorber（1）The heat of middle cooling water is cooled down.
7. a kind of lithium bromide adsorption water chilling machine set system of band evaporation cooling heat exchange device according to claim 6,
It is characterized in that：The absorber（1）Cooling water inlet（A）And cooling water outlet（B）Pipeline on setting evaporation cooling heat transferring
Device two（16）And cooling water circulating pump（22）, evaporate cooling heat exchange device two（16）Connect water circulating pump two（18）.
8. a kind of lithium bromide adsorption water chilling machine set system of band evaporation cooling heat exchange device according to claim 6,
It is characterized in that：The evaporation cooling heat exchange device two（16）Header tank two（17）Air intlet two is arranged in top（L）, evaporate cold
But heat-exchanger rig two（16）Top be provided with wind exhausting outlet two（M）, wind exhausting outlet two（M）Place is provided with for cooling down to evaporation
Heat-exchanger rig two（16）External air draft blower two（21）, evaporate cooling heat exchange device two（16）Air-cooled side can also be used
Formula, i.e. evaporation cooling heat exchange device two（16）By cooling coil two（20）, blower two（21）Composition, no setting is required header tank two
（17）, circulating sprayer two（19）And water circulating pump two（18）.
9. the lithium bromide adsorption water chilling machine system of -8 any a kind of band evaporation cooling heat exchange devices according to claim 1
System, it is characterised in that：The water chilling unit system is suitable for warm water type, direct combustion type, steam type, flue gas type and compound energy type
Lithium bromide adsorption water chilling unit.
10. the lithium bromide adsorption water chilling unit of -8 any a kind of band evaporation cooling heat exchange devices according to claim 1
System, it is characterised in that：The water chilling unit system is suitable for single-effect lithiumbromide absorption chiller and dual effect type bromination
Lithium-absorbing formula water cooler.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820437677.5U CN208108535U (en) | 2018-03-29 | 2018-03-29 | A kind of lithium bromide adsorption water chilling machine set system of band evaporation cooling heat exchange device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820437677.5U CN208108535U (en) | 2018-03-29 | 2018-03-29 | A kind of lithium bromide adsorption water chilling machine set system of band evaporation cooling heat exchange device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208108535U true CN208108535U (en) | 2018-11-16 |
Family
ID=64123213
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820437677.5U Active CN208108535U (en) | 2018-03-29 | 2018-03-29 | A kind of lithium bromide adsorption water chilling machine set system of band evaporation cooling heat exchange device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208108535U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113737209A (en) * | 2021-09-27 | 2021-12-03 | 长江勘测规划设计研究有限责任公司 | Water electrolysis hydrogen production system adopting external circulation evaporation cooling full immersion and use method |
-
2018
- 2018-03-29 CN CN201820437677.5U patent/CN208108535U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113737209A (en) * | 2021-09-27 | 2021-12-03 | 长江勘测规划设计研究有限责任公司 | Water electrolysis hydrogen production system adopting external circulation evaporation cooling full immersion and use method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN201152648Y (en) | Falling film evaporative cooling refrigeration set | |
| CN106091187B (en) | A kind of absorption coupling air-conditioning device of low-temperature heat source and regulation method | |
| CN101634476B (en) | Closed evaporation cooling high-temperature cold water unit | |
| CN102506564B (en) | Condensation water residual heat first-effect flash evaporation natural air dehumidifying, preheating and drying baking oven system | |
| CN102052799A (en) | Device for producing low-temperature water by using waste heat | |
| CN206037294U (en) | Two -stage cooling solution humidifying unit that cooling tower and heat pump system combine | |
| CN105953459B (en) | A kind of single-double effect compound type absorption refrigeration unit | |
| CN201535592U (en) | Lithium bromide absorption water chilling unit adopting falling film generator | |
| CN206247691U (en) | Superposition type solution series double-effect lithium bromide absorption type refrigerating heat pump unit | |
| CN208108535U (en) | A kind of lithium bromide adsorption water chilling machine set system of band evaporation cooling heat exchange device | |
| CN105318461A (en) | Open-closed difunctional heat-source tower | |
| CN207180090U (en) | A kind of gas internal-combustion engine drives double-effect lithium bromide absorption type heat pump assembly | |
| CN205690733U (en) | A kind of single-double effect compound type absorption refrigeration unit | |
| CN204063674U (en) | Lithium bromide absorption refrigerating set | |
| CN205332427U (en) | Salt solution double -cold -source fresh air unit | |
| CN206247687U (en) | Superposition type solution connection in series-parallel double-effect lithium bromide absorption type refrigerating heat pump unit | |
| CN100402951C (en) | Steam or hot water type lithium bromide absorption cooling and warming water machine | |
| CN209054806U (en) | A kind of air cooled condenser suitable for lithium bromide absorption refrigerating set | |
| CN112413925A (en) | Low-temperature heat source refrigerating device | |
| CN203375765U (en) | Absorption heat pump unit | |
| CN208222914U (en) | A kind of superconduction cumulative heat pump system | |
| CN206247688U (en) | Superposition type solution parallel double-effect lithium bromide absorption type refrigeration heat pump unit | |
| CN206771609U (en) | The air-cooled cold wind solar airconditioning unit of suction-type lithium bromide | |
| CN114111023A (en) | Refrigerating and heating double-effect heat exchanger with natural cooling function and control method thereof | |
| CN206247686U (en) | Superposition type solution parallel connection mono-potency lithium bromide absorption type refrigeration heat pump unit |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |