CN203719224U - Direct-combustion lithium bromide absorption cold and hot water unit used for producing high-temperature hot water - Google Patents
Direct-combustion lithium bromide absorption cold and hot water unit used for producing high-temperature hot water Download PDFInfo
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- CN203719224U CN203719224U CN201420071451.XU CN201420071451U CN203719224U CN 203719224 U CN203719224 U CN 203719224U CN 201420071451 U CN201420071451 U CN 201420071451U CN 203719224 U CN203719224 U CN 203719224U
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- temperature
- solution
- hot water
- direct
- lithium bromide
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- 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
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
- Y02B30/62—Absorption based systems
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- Sorption Type Refrigeration Machines (AREA)
Abstract
The utility model relates to a direct-combustion lithium bromide absorption cold and hot water unit used for producing high-temperature hot water and belongs to the technical field of air conditioning equipment. The direct-combustion lithium bromide absorption cold and hot water unit used for producing the high-temperature hot water comprises a direct-combustion high pressure generator (1), a low pressure generator (9), a condenser (8), an evaporator (5), an absorber (4), a low temperature solution heat exchanger (3), a high temperature solution heat exchanger (2), a solution pump (6) and a cryogen pump (7), wherein a solution communication pipe (14) is additionally arranged between a solution pump outlet pipeline (10) and an evaporator cryogen water bag (11); a solution switch valve (15) is arranged on the solution communication pipe (14). According to the flow, the temperature of dilute solution is no more than 10 DEG C higher than the temperature of a heating hot water outlet under a heating work condition, the temperature is reduced by about 40 DEG C in comparison with a traditional mode, when the high-temperature hot water is produced, the solution temperature is effectively controlled, the operation reliability is improved, the exhaust gas temperature is reduced by 40 DEG C, the fuel consumption is reduced by about 2 %, the energy utilization rate is improved, and the thermal pollution of exhaust gas to the environment is reduced.
Description
Technical field
The utility model relates to a kind of direct-burning lithium bromide absorption cold-hot water assembing group.Belong to air conditioner technical field.
Background technology
Direct combustion type dual effect type cold/hot water machine of lithium bromide group as shown in Figure 1, is made up of the pipeline of direct combustion high pressure generator 1, low pressure generator 9, condenser 8, evaporimeter 5, absorber 5, cryogenic fluid heat exchanger 3, high-temperature solution heat exchanger 2, heating solution transfer valve 12, heating refrigerant vapour transfer valve 13, solution pump 6, cryogenic fluid pump 7, valve, control system (not shown) and connecting components at present.When unit moves in heating operating mode, heating solution transfer valve 12 and heating refrigerant vapour transfer valve 13 are opened, cryogenic fluid pump and external system cooling water pump stop, the low-temperature water heating coming from air conditioner user enters in heat exchange pipe of evaporator, the heat of condensation of the water vapour being produced by heat exchange pipe external surface direct combustion high pressure generator heat dilute solution heats, temperature is sent to heating user after raising, the water as refrigerant that solution after direct combustion high pressure generator is concentrated enters in absorber and after condensing is mixed into weak solution, is again circulated and heats toward direct combustion high pressure generator from solution pumping.When heating water outlet reaches 60 DEG C, solution temperature reaches 110 DEG C of left and right, 50 DEG C of left and right of heating hot water and the solution temperature difference.In the time that needs are produced more than 70 DEG C high temperature heating water, may exceed the resistance to extreme temperature of existing solution pump, operational reliability reduces greatly.Another direct combustion high pressure generator exhaust gas temperature rises, heating decrease in efficiency.Produce at present high temperature heating hot water and conventionally adopt flow process as shown in Figure 2, on traditional direct combustion high pressure generator, heating hot water heat exchanger 16 is set.In the time of heating operation, heating solution transfer valve and heating refrigerant vapour transfer valve to be closed, the independent similar boiler operatiopn of direct combustion high pressure generator, produces refrigerant vapour and enters heating hot water heat exchanger heating water, and the solidifying water of refrigerant vapour is got back to direct combustion high pressure generator.Which systematic comparison complexity, cost is high, while producing high temperature heating water, because solution temperature is higher, causes exhaust gas temperature higher, affects the heating thermal efficiency.How to find the novel direct-burning lithium bromide absorption cold-hot water assembing of producing high-temperature-hot-water that a kind of effective reduction solution running temperature, system are simple, heating efficiency is high to consist of one of important topic of current research.
Utility model content
The purpose of this utility model is to overcome above-mentioned deficiency, and the direct-burning lithium bromide absorption cold-hot water assembing group of producing high-temperature-hot-water that a kind of effective reduction solution running temperature, system are simple, heating efficiency is high is provided.
The purpose of this utility model is achieved in that a kind of direct-burning lithium bromide absorption cold-hot water assembing group of producing high-temperature-hot-water, comprise direct combustion high pressure generator, low pressure generator, condenser, evaporimeter, absorber, cryogenic fluid heat exchanger, high-temperature solution heat exchanger, solution pump and cryogenic fluid pump, between solution pump discharge pipeline and evaporimeter water as refrigerant liquid capsule, set up a solution communicating pipe, solution transfer valve was set on solution communicating pipe.
In the time that heating operating mode is moved, solution transfer valve is opened, solution pump discharge solution is divided into two tunnels, it is concentrated that one tunnel enters high pressure generator heating, separately leads up to and enter evaporimeter liquid capsule solution communicating pipe, makes the liquid in evaporimeter liquid capsule become weak solution from original water as refrigerant, open cryogenic fluid pump, weak solution in evaporimeter liquid capsule is evenly distributed to outside heat-transfer pipe of evaporator, and lithium-bromide solution is emitted the heat of condensation of refrigerant vapour, the hot water that heating is flowed through in heat-transfer pipe of evaporator in the time absorbing refrigerant vapour.
The beneficial effects of the utility model are:
The utility model is by above-mentioned flow process, under heating operating mode, weak solution temperature is higher than in 10 DEG C of heating hot water outlet temperatures, reduce by 40 DEG C of left and right than traditional approach, while producing high-temperature-hot-water, solution temperature is effectively controlled, and has improved operational reliability, exhaust gas temperature reduces by 40 DEG C simultaneously, fuel consumption 2% left and right that declines, improves energy utilization rate, and has reduced the thermal pollution of smoke evacuation to environment.
Brief description of the drawings
Fig. 1 is direct combustion dual effect type cold/hot water machine of lithium bromide group schematic diagram in the past.
Fig. 2 was for produced high-temperature-hot-water direct combustion dual effect type cold/hot water machine of lithium bromide group intention in the past.
Fig. 3 is the direct-burning lithium bromide absorption cold-hot water assembing group schematic diagram that the utility model is produced high-temperature-hot-water.
Reference numeral:
Direct combustion high pressure generator 1
High-temperature solution heat exchanger 2
Cryogenic fluid heat exchanger 3
Absorber 4
Evaporimeter 5
Solution pump 6
Cryogenic fluid pump 7
Condenser 8
Low pressure generator 9
Solution pump discharge pipe 10
Evaporimeter water as refrigerant liquid capsule 11
Heating solution transfer valve 12
Heating refrigerant vapour transfer valve 13
Solution communicating pipe 14
Solution transfer valve 15
Heating hot water heat exchanger 16.
Detailed description of the invention
As shown in Figure 3, by comprising direct combustion high pressure generator 1, low pressure generator 9, condenser 8, evaporimeter 5, absorber 4, cryogenic fluid heat exchanger 3, high-temperature solution heat exchanger 2, solution pump 6, cryogenic fluid pump 7, heating solution transfer valve 12, heating refrigerant vapour transfer valve 13, on the basis of traditional direct-burning lithium bromide absorption cold-hot water assembing group of the composition such as the pipeline of control system (not shown) and connecting components, between solution pump discharge pipeline 10 and evaporimeter water as refrigerant liquid capsule 11, set up a solution communicating pipe 14, solution transfer valve 15 was set on solution communicating pipe 14.
Above scheme is applicable to evaporimeter-absorber and can is single hop (shown in figure), also can is two sections or multistage, and cooling water can be that parallel-connection flow can be also serial flow.
Claims (3)
1. produce the direct-burning lithium bromide absorption cold-hot water assembing group of high-temperature-hot-water for one kind, comprise direct combustion high pressure generator (1), low pressure generator (9), condenser (8), evaporimeter (5), absorber (4), cryogenic fluid heat exchanger (3), high-temperature solution heat exchanger (2), solution pump (6) and cryogenic fluid pump (7), it is characterized in that: between solution pump discharge pipeline (10) and evaporimeter water as refrigerant liquid capsule (11), set up a solution communicating pipe (14), solution transfer valve (15) was set on solution communicating pipe (14).
2. a kind of direct-burning lithium bromide absorption cold-hot water assembing group of producing high-temperature-hot-water according to claim 1, is characterized in that: the evaporimeter (5) of described unit and absorber (4) are single hop, two sections or multistage.
3. a kind of direct-burning lithium bromide absorption cold-hot water assembing group of producing high-temperature-hot-water according to claim 1, is characterized in that: the cooling water of described unit is parallel-connection flow or serial flow.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420071451.XU CN203719224U (en) | 2014-02-19 | 2014-02-19 | Direct-combustion lithium bromide absorption cold and hot water unit used for producing high-temperature hot water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420071451.XU CN203719224U (en) | 2014-02-19 | 2014-02-19 | Direct-combustion lithium bromide absorption cold and hot water unit used for producing high-temperature hot water |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203719224U true CN203719224U (en) | 2014-07-16 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420071451.XU Expired - Fee Related CN203719224U (en) | 2014-02-19 | 2014-02-19 | Direct-combustion lithium bromide absorption cold and hot water unit used for producing high-temperature hot water |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203719224U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103822395A (en) * | 2014-02-19 | 2014-05-28 | 双良节能系统股份有限公司 | Direct-fired lithium bromide absorbing typed cold and hot water unit for producing high temperature hot water |
| CN109458753A (en) * | 2018-12-27 | 2019-03-12 | 双良节能系统股份有限公司 | A kind of on-line checking density flue gas type suction-type lithium bromide low-temperature cold water unit |
-
2014
- 2014-02-19 CN CN201420071451.XU patent/CN203719224U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103822395A (en) * | 2014-02-19 | 2014-05-28 | 双良节能系统股份有限公司 | Direct-fired lithium bromide absorbing typed cold and hot water unit for producing high temperature hot water |
| CN109458753A (en) * | 2018-12-27 | 2019-03-12 | 双良节能系统股份有限公司 | A kind of on-line checking density flue gas type suction-type lithium bromide low-temperature cold water unit |
| CN109458753B (en) * | 2018-12-27 | 2024-04-02 | 双良节能系统股份有限公司 | Online detection density flue gas type lithium bromide absorption type low-temperature water chilling unit |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140716 Termination date: 20220219 |