CN205747579U - Changes in temperature simultaneous type cold/hot water machine of lithium bromide group with double cigarette heat regenerator - Google Patents
Changes in temperature simultaneous type cold/hot water machine of lithium bromide group with double cigarette heat regenerator Download PDFInfo
- Publication number
- CN205747579U CN205747579U CN201620527307.1U CN201620527307U CN205747579U CN 205747579 U CN205747579 U CN 205747579U CN 201620527307 U CN201620527307 U CN 201620527307U CN 205747579 U CN205747579 U CN 205747579U
- Authority
- CN
- China
- Prior art keywords
- recovery device
- heat recovery
- exhaust heat
- temperature
- regenerator
- 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.)
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 51
- AMXOYNBUYSYVKV-UHFFFAOYSA-M lithium bromide Chemical group [Li+].[Br-] AMXOYNBUYSYVKV-UHFFFAOYSA-M 0.000 title claims abstract description 34
- 235000019504 cigarettes Nutrition 0.000 title claims abstract description 12
- 238000011084 recovery Methods 0.000 claims abstract description 59
- 239000000779 smoke Substances 0.000 claims abstract description 21
- 239000006096 absorbing agent Substances 0.000 claims abstract description 17
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 14
- 239000003546 flue gas Substances 0.000 claims abstract description 14
- 230000015572 biosynthetic process Effects 0.000 claims abstract description 3
- 239000006200 vaporizer Substances 0.000 claims description 6
- 238000007599 discharging Methods 0.000 abstract description 7
- 239000003517 fume Substances 0.000 abstract description 6
- 239000007789 gas Substances 0.000 abstract description 2
- 229940059936 lithium bromide Drugs 0.000 description 9
- 238000002485 combustion reaction Methods 0.000 description 6
- 238000010438 heat treatment Methods 0.000 description 6
- 239000000446 fuel Substances 0.000 description 4
- 238000005057 refrigeration Methods 0.000 description 4
- 239000012530 fluid Substances 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- 239000000498 cooling water Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000003507 refrigerant Substances 0.000 description 2
- 239000002918 waste heat Substances 0.000 description 2
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000031709 bromination Effects 0.000 description 1
- 238000005893 bromination reaction Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229910052744 lithium Inorganic materials 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
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
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P80/00—Climate change mitigation technologies for sector-wide applications
- Y02P80/10—Efficient use of energy, e.g. using compressed air or pressurized fluid as energy carrier
- Y02P80/15—On-site combined power, heat or cool generation or distribution, e.g. combined heat and power [CHP] supply
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Abstract
This utility model belongs to air conditioner technical field, relates to a kind of changes in temperature simultaneous type cold/hot water machine of lithium bromide group with double cigarette heat regenerator.This water chiller-heater unit, weak solution pump is set below absorber, weak solution delivery side of pump pipeline divides two-way, one tunnel connects low temperature heat exchanger, another road connects cryogen and coagulates hydro-thermal retracting device, the connection formation of two-way output pipe is confluxed pipeline, the pipeline that confluxes connects high-temperature heat exchanger, the smoke evacuation outlet of high-temp regenerator has been arranged in series exhaust heat recovery device I, greenhouse water heater is set on high-temp regenerator, exhaust heat recovery device I is arranged in series with exhaust heat recovery device II, high-temp regenerator discharge flue gas respectively in exhaust heat recovery device I with weak solution heat exchange, with greenhouse warm water heat exchange in exhaust heat recovery device II, realize reducing exhaust gas temperature, reduce the purpose of greenhouse water heater heat exchange area.The recyclable a large amount of fume afterheats of this utility model, improve energy utilization rate, reduce the smoke discharging residual heat thermal pollution to environment.
Description
Technical field
This utility model belongs to air conditioner technical field, is specifically related to a kind of changes in temperature with double cigarette heat regenerator simultaneously
Type cold/hot water machine of lithium bromide group.
Background technology
At present direct combustion changes in temperature simultaneous type cold/hot water machine of lithium bromide group as it is shown in figure 1, by absorber 1, vaporizer 2,
Condenser 3, low-temperature regenerator 4, high-temp regenerator 5, low temperature heat exchanger 6, high-temperature heat exchanger 7, cryogen coagulate hydro-thermal and reclaim dress
Put 8, cryogenic fluid pump 9, weak solution pump 10 and concentrated solution pump 11, greenhouse water heater 12, valve, control system and the pipe of connecting components
Road is constituted.Operationally, the lithium bromide weak solution in absorber 1 is sent to cryogen by weak solution pump 10 and coagulates hydro-thermal retracting device unit
8, after low temperature heat exchanger 6, high-temperature heat exchanger 7, temperature raises, and enters back into high-temp regenerator 5, low-temperature regenerator 4 becomes bromination
Lithium concentrated solution, finally returns absorber 1.
Unit temperature by high-temp regenerator in operation process restricts, and flue gas exit temperature is higher, discharges fume during refrigeration
Temperature about 200 DEG C, exhaust gas temperature about 170 DEG C during heating, fail to make full use of smoke discharging residual heat and carry out heating and refrigeration, smoke evacuation
Waste heat can only discharge in vain, causes the waste of a large amount of fume afterheat, produces the thermal pollution of discharge simultaneously.Use common direct heat transfer
Technology is difficult to reclaim this part of waste heat, the most fully recycles direct fired lithium bromide absorption type chiller smoke discharging residual heat,
Improve the heat exchange efficiency of unit, it is achieved the economic benefit of energy-saving and emission-reduction and social benefit, become at present research important topic it
One.
Summary of the invention
For solving problem above, this utility model provides a kind of changes in temperature simultaneous type lithium bromide with double cigarette heat regenerator to inhale
Receipts formula water chiller-heater unit, by being arranged in series exhaust heat recovery device I and exhaust heat recovery device II in high-temp regenerator smoke evacuation outlet,
The flue gas making high-temp regenerator discharge successively enters exhaust heat recovery device I and exhaust heat recovery device II, respectively at exhaust heat recovery
In device I with weak solution heat exchange, in exhaust heat recovery device II with greenhouse warm water heat exchange, it is achieved direct combustion changes in temperature simultaneous type lithium bromide inhale
Effective utilization of receipts formula water chiller-heater unit smoke discharging residual heat, reduces the waste of fume afterheat, reduces greenhouse water heater heat-transfer surface simultaneously
Long-pending, improve the heat exchange efficiency of unit, it is possible to decrease unit fuel consumption, improve energy utilization rate, reduce smoke discharging residual heat to environment
Thermal pollution, it is achieved the economic benefit of energy-saving and emission-reduction and social benefit.
The technical scheme is that a kind of changes in temperature with double cigarette heat regenerator of this utility model
Simultaneous type cold/hot water machine of lithium bromide group, absorber is connected with condenser, and absorber is connected with vaporizer, below absorber
Being provided with the weak solution pump for lithium bromide circulation, weak solution delivery side of pump pipeline divides two-way, and a road connects low temperature heat exchanger,
Another road connects cryogen and coagulates hydro-thermal retracting device, and cryogen coagulates the output pipe of hydro-thermal retracting device and the output of low temperature heat exchanger
Pipeline connection forms the pipeline that confluxes, and the pipeline that confluxes connects high-temperature heat exchanger, and the smoke evacuation outlet of high-temp regenerator has been arranged in series
Exhaust heat recovery device I, exhaust heat recovery device I is arranged in series with high temperature exchanger；Greenhouse water heater is set on high-temp regenerator, warm
Room water heater is arranged in series with exhaust heat recovery device II；Exhaust heat recovery device I is arranged in series with exhaust heat recovery device II, makes high temperature
The flue gas of regenerator discharge successively enters exhaust heat recovery device I and exhaust heat recovery device II, respectively in exhaust heat recovery device I with
Weak solution heat exchange, in exhaust heat recovery device II with greenhouse warm water heat exchange.
Described exhaust heat recovery device I connects solution pipe arrangement T1, and solution pipe arrangement T1 is provided with solution bypass pipe arrangement T2.
It is provided with valve F5 on described solution pipe arrangement T1, solution bypass pipe arrangement T2 is provided with valve F4.
The beneficial effects of the utility model are: by tradition direct combustion changes in temperature simultaneous type cold/hot water machine of lithium bromide group
On the basis of, it is arranged in series exhaust heat recovery device I and exhaust heat recovery device II in high-temp regenerator smoke evacuation outlet, makes high-temp regenerator
The flue gas of discharge successively enters exhaust heat recovery device I and exhaust heat recovery device II, respectively in exhaust heat recovery device I with weak solution
Heat exchange, in exhaust heat recovery device II with greenhouse warm water heat exchange.Tradition direct combustion changes in temperature simultaneous type cold/hot water machine of lithium bromide
The flue-gas temperature about 200 DEG C of group high-temp regenerator discharge, after exhaust heat recovery device I, flue-gas temperature is reduced to 150 DEG C of left sides
The right side, then after exhaust heat recovery device II, flue-gas temperature can be reduced to about 70 DEG C, recyclable a large amount of fume afterheats, is not increasing
On the premise of fuel consumption, unit refrigeration or heating ability and capacity factor is made to improve；In identical refrigeration or heating ability
Under premise, it is possible to decrease unit fuel consumption, to reduce the purpose of operating cost, improve energy utilization rate, reduce smoke evacuation remaining
The heat thermal pollution to environment, it is achieved the economic benefit of energy-saving and emission-reduction and social benefit.
Accompanying drawing explanation
Fig. 1 is tradition direct combustion changes in temperature simultaneous type cold/hot water machine of lithium bromide group flow chart；
Fig. 2 is the changes in temperature simultaneous type cold/hot water machine of lithium bromide group structure of this utility model band double cigarette heat regenerator
Schematic diagram；
In figure: 1-absorber, 2-vaporizer, 3-condenser, 4-low-temperature regenerator, 5-high-temp regenerator, 6-Low Temperature Thermal is handed over
Parallel operation, 7-high-temperature heat exchanger, 8-cryogen coagulates hydro-thermal retracting device, 9-cryogenic fluid pump, 10-weak solution pump, 11-concentrated solution pump, 12-
Greenhouse water heater, 13-valve F1,14-valve F2,15-valve F3,16-valve F4,17-valve F5,18-solution pipe arrangement T1,
19-solution bypass pipe arrangement T2,20-exhaust heat recovery device I, 21-exhaust heat recovery device II, a, smoke evacuation outlet, b, cooling water inlet,
C, coolant outlet, d, cooling water outlet, e, cold water inlet, f, driving heat source, g, warm water entrance, h, warm water export.
Detailed description of the invention
Below in conjunction with the accompanying drawings this utility model is further illustrated, but this utility model is not limited to specific embodiment.
Embodiment
The changes in temperature simultaneous type cold/hot water machine of lithium bromide group with double cigarette heat regenerator as shown in Figure 2, including inhaling
Receive device 1, vaporizer 2, condenser 3, low-temperature regenerator 4, high-temp regenerator 5, low temperature heat exchanger 6, high-temperature heat exchanger 7, cold
Hydro-thermal retracting device 8, cryogenic fluid pump 9, weak solution pump 10 and concentrated solution pump 11, greenhouse water heater 12, exhaust heat recovery device I are coagulated in agent
20, the pipeline of exhaust heat recovery device II 21, valve, control system and connecting components.
Absorber 1 is connected with condenser 3, and absorber 1 is connected with vaporizer 2, is provided with for lithium bromide below absorber 1
The weak solution pump 10 of circulation, the export pipeline of weak solution pump 10 divides two-way, and a road connects low temperature heat exchanger 6, and another road connects
Cryogen coagulates hydro-thermal retracting device 8, and the output pipe of output pipe and low temperature heat exchanger 6 that cryogen coagulates hydro-thermal retracting device 8 connects
Logical formation is confluxed pipeline, and the pipeline that confluxes connects high-temperature heat exchanger 7, and the smoke evacuation outlet a of high-temp regenerator 5 has been arranged in series smoke evacuation
Heat regenerator I 20, exhaust heat recovery device I 20 is arranged in series with high temperature exchanger 7；Greenhouse warm water is set on high-temp regenerator 5
Device 12, greenhouse water heater 12 is arranged in series with exhaust heat recovery device II 21；Exhaust heat recovery device I 20 and exhaust heat recovery device II
21 are arranged in series, and the flue gas making high-temp regenerator 5 discharge successively enters exhaust heat recovery device I 20 and exhaust heat recovery device II
21, respectively in exhaust heat recovery device I 20 with weak solution heat exchange, in exhaust heat recovery device II 21 with greenhouse warm water heat exchange.
Described exhaust heat recovery device I 20 connects solution pipe arrangement T1 18, and solution pipe arrangement T1 18 is provided with solution bypass
Pipe arrangement T2 19.
It is provided with valve F5 17 on described solution pipe arrangement T1 18, solution bypass pipe arrangement T2 19 is provided with valve F4
16.When exhaust heat recovery device I 20 blocks, solution bypass can be carried out by solution bypass pipe arrangement T2 19.
Wherein absorber 1, low temperature heat exchanger 6, high-temperature heat exchanger 7, cryogen coagulate hydro-thermal retracting device 8, low-temp recovery
The composition lithium-bromide solution circulation of device 4, high-temp regenerator 5, exhaust heat recovery device I 20, i.e. dilute from absorber 1 lithium bromide out
Solution is sent to cryogen by weak solution pump 10 1 tunnel and coagulates hydro-thermal retracting device 8, and low temperature heat exchanger 6 is sent on another road, and two-way is dilute
Solution enters high-temperature heat exchanger 7 after cryogen coagulates hydro-thermal retracting device 8 and low temperature heat exchanger 6 confluxes, subsequently into smoke evacuation
The flue gas heat exchange that heat regenerator I 20 is discharged with high-temp regenerator 5, enters back into high-temp regenerator 5, dilute molten in high-temp regenerator 5
Liquid is heated, and is condensed into intermediate concentration solution；Intermediate concentration solution, through high-temperature heat exchanger 7, enters low-temperature regenerator 4, is come
The refrigerant vapour heating produced in high-temp regenerator 5, becomes concentrated solution；Concentrated solution is temperature fall after low temperature heat exchanger 6
Low, eventually pass back to absorber 1.
Arranging greenhouse water heater 12 on high-temp regenerator 5, greenhouse water heater 12 is connected with exhaust heat recovery device II 21 and is set
Putting, warm water entrance g is arranged on exhaust heat recovery device II 21, and warm water outlet h is arranged on greenhouse water heater 12, and warm water is row
Entering greenhouse water heater 12 after being heated by high-temperature flue gas in cigarette heat regenerator II 21, the warm water entering greenhouse water heater 12 is high
The refrigerant vapour heating that temperature regenerator 5 produces.By being arranged in series exhaust heat recovery device I at the smoke evacuation of high-temp regenerator 5 outlet a
20 and exhaust heat recovery device II 21, the flue gas making high-temp regenerator 5 discharge successively enters exhaust heat recovery device I 20 and smoke evacuation heat
Withdrawer II 21, respectively in exhaust heat recovery device I 20 with weak solution heat exchange, in exhaust heat recovery device II 21 with greenhouse
Warm water heat exchange.
This utility model realizes effective utilization of direct combustion changes in temperature simultaneous type cold/hot water machine of lithium bromide group smoke discharging residual heat,
Reduce the waste of fume afterheat, reduce the heat exchange area of greenhouse water heater 12 simultaneously, improve the heat exchange efficiency of unit, it is possible to decrease machine
Group fuel consumption, improve energy utilization rate, reduce the smoke discharging residual heat thermal pollution to environment, it is achieved the economic benefit of energy-saving and emission-reduction and
Social benefit.
Above content is to combine concrete optimal technical scheme further detailed description of the utility model, it is impossible to
Assert that of the present utility model being embodied as is confined to these explanations.For this utility model art, without departing from
On the premise of this utility model design, it is also possible to make some simple deduction or replace, all should be considered as belonging to this utility model
Protection domain.
Claims (3)
1. the changes in temperature simultaneous type cold/hot water machine of lithium bromide group with double cigarette heat regenerator, absorber (1) and condenser (3)
Connecting, absorber (1) is connected with vaporizer (2), and absorber (1) lower section is provided with the weak solution pump for lithium bromide circulation
(10), the export pipeline of weak solution pump (10) divides two-way, and a road connects low temperature heat exchanger (6), and another road connects cryogen and coagulates water
Heat reclamation device (8), the output pipe of output pipe and low temperature heat exchanger (6) that cryogen coagulates hydro-thermal retracting device (8) connects
Formation is confluxed pipeline, and the pipeline that confluxes connects high-temperature heat exchanger (7), and high-temp regenerator (5) arranges greenhouse water heater (12), its
It is characterised by: the smoke evacuation outlet of high-temp regenerator (5) has been arranged in series exhaust heat recovery device I (20), exhaust heat recovery device I (20)
Being arranged in series with high temperature exchanger (7), the flue gas of direct fired machine discharge changes with weak solution in exhaust heat recovery device I (20)
Heat；Greenhouse water heater (12) is arranged in series with exhaust heat recovery device II (21), and the flue gas of direct fired machine discharge returns in smoke evacuation heat
With greenhouse warm water heat exchange in receipts device II (21)；Exhaust heat recovery device I (20) is arranged in series with exhaust heat recovery device II (21).
The changes in temperature simultaneous type cold/hot water machine of lithium bromide group of band the most according to claim 1 double cigarette heat regenerator,
It is characterized in that: described exhaust heat recovery device I (20) connect solution pipe arrangement T1(18), solution pipe arrangement T1(18) on be provided with solution
Bypass pipe arrangement T2(19).
The changes in temperature simultaneous type cold/hot water machine of lithium bromide group of band the most according to claim 2 double cigarette heat regenerator,
It is characterized in that: described solution pipe arrangement T1(18) on be provided with valve F5(17), solution bypass pipe arrangement T2(19) on be provided with valve
Door F4(16).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620527307.1U CN205747579U (en) | 2016-06-02 | 2016-06-02 | Changes in temperature simultaneous type cold/hot water machine of lithium bromide group with double cigarette heat regenerator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620527307.1U CN205747579U (en) | 2016-06-02 | 2016-06-02 | Changes in temperature simultaneous type cold/hot water machine of lithium bromide group with double cigarette heat regenerator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205747579U true CN205747579U (en) | 2016-11-30 |
Family
ID=57359710
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620527307.1U Expired - Fee Related CN205747579U (en) | 2016-06-02 | 2016-06-02 | Changes in temperature simultaneous type cold/hot water machine of lithium bromide group with double cigarette heat regenerator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205747579U (en) |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108362035A (en) * | 2018-04-09 | 2018-08-03 | 双良节能系统股份有限公司 | Eliminating white smoke efficient direct-burning lithium bromide absorption cold, Hot water units system |
| CN108362034A (en) * | 2018-04-09 | 2018-08-03 | 双良节能系统股份有限公司 | A kind of environment-friendly high-efficiency flue gas type lithium bromide absorption cold, Hot water units |
| CN108397932A (en) * | 2018-04-09 | 2018-08-14 | 双良节能系统股份有限公司 | A kind of environmental protection band health hot water direct-burning type lithium bromide absorption type hot water or cold water's unit |
| CN108397930A (en) * | 2018-04-09 | 2018-08-14 | 双良节能系统股份有限公司 | Eliminating white smoke efficient direct-burning lithium bromide absorption cold, Hot water units |
| CN108397931A (en) * | 2018-04-09 | 2018-08-14 | 双良节能系统股份有限公司 | A kind of environment-friendly high-efficiency energy-saving direct-burning type lithium bromide absorption type hot water or cold water's unit |
| CN108489142A (en) * | 2018-04-09 | 2018-09-04 | 双良节能系统股份有限公司 | A kind of environment-friendly high-efficiency direct-burning type lithium bromide absorption type hot water or cold water's machine set system |
| CN108507223A (en) * | 2018-04-09 | 2018-09-07 | 双良节能系统股份有限公司 | Eliminating white smoke high effective flue gas type lithium bromide absorption cold, Hot water units |
| CN108518886A (en) * | 2018-04-09 | 2018-09-11 | 双良节能系统股份有限公司 | Eliminating white smoke high effective flue gas hot water type lithium bromide absorption cooling, Hot water units |
| CN108518891A (en) * | 2018-04-09 | 2018-09-11 | 双良节能系统股份有限公司 | Eliminating white smoke band health hot water direct-burning type lithium bromide absorption type hot water or cold water's unit |
| CN108518885A (en) * | 2018-04-09 | 2018-09-11 | 双良节能系统股份有限公司 | A kind of environment-friendly high-efficiency fume hot-water type lithium bromide absorption cold, Hot water units |
-
2016
- 2016-06-02 CN CN201620527307.1U patent/CN205747579U/en not_active Expired - Fee Related
Cited By (20)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108362035A (en) * | 2018-04-09 | 2018-08-03 | 双良节能系统股份有限公司 | Eliminating white smoke efficient direct-burning lithium bromide absorption cold, Hot water units system |
| CN108362034A (en) * | 2018-04-09 | 2018-08-03 | 双良节能系统股份有限公司 | A kind of environment-friendly high-efficiency flue gas type lithium bromide absorption cold, Hot water units |
| CN108397932A (en) * | 2018-04-09 | 2018-08-14 | 双良节能系统股份有限公司 | A kind of environmental protection band health hot water direct-burning type lithium bromide absorption type hot water or cold water's unit |
| CN108397930A (en) * | 2018-04-09 | 2018-08-14 | 双良节能系统股份有限公司 | Eliminating white smoke efficient direct-burning lithium bromide absorption cold, Hot water units |
| CN108397931A (en) * | 2018-04-09 | 2018-08-14 | 双良节能系统股份有限公司 | A kind of environment-friendly high-efficiency energy-saving direct-burning type lithium bromide absorption type hot water or cold water's unit |
| CN108489142A (en) * | 2018-04-09 | 2018-09-04 | 双良节能系统股份有限公司 | A kind of environment-friendly high-efficiency direct-burning type lithium bromide absorption type hot water or cold water's machine set system |
| CN108507223A (en) * | 2018-04-09 | 2018-09-07 | 双良节能系统股份有限公司 | Eliminating white smoke high effective flue gas type lithium bromide absorption cold, Hot water units |
| CN108518886A (en) * | 2018-04-09 | 2018-09-11 | 双良节能系统股份有限公司 | Eliminating white smoke high effective flue gas hot water type lithium bromide absorption cooling, Hot water units |
| CN108518891A (en) * | 2018-04-09 | 2018-09-11 | 双良节能系统股份有限公司 | Eliminating white smoke band health hot water direct-burning type lithium bromide absorption type hot water or cold water's unit |
| CN108518885A (en) * | 2018-04-09 | 2018-09-11 | 双良节能系统股份有限公司 | A kind of environment-friendly high-efficiency fume hot-water type lithium bromide absorption cold, Hot water units |
| CN108397931B (en) * | 2018-04-09 | 2023-12-15 | 双良节能系统股份有限公司 | Environment-friendly, efficient and energy-saving direct-fired lithium bromide absorption type cold and hot water unit |
| CN108397930B (en) * | 2018-04-09 | 2024-01-05 | 双良节能系统股份有限公司 | White smoke-eliminating high-efficiency direct-combustion lithium bromide absorption type cold and hot water unit |
| CN108362035B (en) * | 2018-04-09 | 2024-01-05 | 双良节能系统股份有限公司 | White smoke-eliminating efficient direct-fired lithium bromide absorption type cold and hot water unit system |
| CN108518885B (en) * | 2018-04-09 | 2024-03-08 | 双良节能系统股份有限公司 | Environment-friendly efficient smoke hot water type lithium bromide absorption type cold and hot water unit |
| CN108362034B (en) * | 2018-04-09 | 2024-03-08 | 双良节能系统股份有限公司 | Environment-friendly and efficient smoke type lithium bromide absorption type cold and hot water unit |
| CN108397932B (en) * | 2018-04-09 | 2024-03-08 | 双良节能系统股份有限公司 | Environment-friendly sanitary hot water direct-fired lithium bromide absorption type cold and hot water unit |
| CN108518891B (en) * | 2018-04-09 | 2024-03-08 | 双良节能系统股份有限公司 | Direct-fired lithium bromide absorption type cold and hot water unit with sanitary hot water for eliminating white smoke |
| CN108518886B (en) * | 2018-04-09 | 2024-03-08 | 双良节能系统股份有限公司 | White smoke-eliminating high-efficiency smoke hot water type lithium bromide absorption type cold and hot water unit |
| CN108507223B (en) * | 2018-04-09 | 2024-03-08 | 双良节能系统股份有限公司 | White smoke eliminating efficient smoke type lithium bromide absorption type cold and hot water unit |
| CN108489142B (en) * | 2018-04-09 | 2024-03-22 | 双良节能系统股份有限公司 | Environment-friendly efficient direct-fired lithium bromide absorption type cold and hot water unit system |
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