CN205403238U - Take gas gas heater's two -period form flue gas hot water type lithium bromide absorbed refrigeration machine - Google Patents
Take gas gas heater's two -period form flue gas hot water type lithium bromide absorbed refrigeration machine Download PDFInfo
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- CN205403238U CN205403238U CN201620153927.3U CN201620153927U CN205403238U CN 205403238 U CN205403238 U CN 205403238U CN 201620153927 U CN201620153927 U CN 201620153927U CN 205403238 U CN205403238 U CN 205403238U
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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 take gas gas heater's two -period form flue gas hot water type lithium bromide absorbed refrigeration machine, its characteristics are: set up low pressure stage evaporimeter (21), low pressure stage absorber (19) and high pressure satage evaporimeter (1), high pressure satage absorber (2) in same evaporator and absorber barrel (25), be provided with evaporating of transversal arrangement between low pressure stage evaporimeter (21), low pressure stage absorber (19) and high pressure satage evaporimeter (1), high pressure satage absorber (2) and inhale segmentation baffle (23), evaporate to inhale and be provided with low pressure stage 0 (42, 43) in segmentation baffle (23), set up steam generator (14), high pressure satage condenser (13) and hot water generator (15), low pressure stage condenser (17) in same emergence condenser cylinder (45), be provided with between steam generator (14), high pressure satage condenser (13) and hot water generator (15), low pressure stage condenser (17) and take place condenser segmentation baffle (44). The utility model discloses solution heat exchanger configuration part is less, simplification solution circuit pipeline.
Description
Technical field
This utility model relates to a kind of lithium-bromide absorption-type refrigerating machine.Belong to air conditioner technical field.
Background technology
Conventional a kind of two-period form fume hot-water type lithium-bromide absorption-type refrigerating machine with flue gas heat-exchange unit two-period form fume hot-water single-double effect compound type lithium bromide absorption type water chiller-heater unit as shown in Figure 1.The two-period form evaporation absorber of this unit adopts left and right segmental structure, and vaporizer includes single effect evaporator 32 and double effect evaporator 35, and absorber includes single effect absorption device 31 and double-effect absorption device 34；Condenser includes low pressure stage condenser 17(and is also called single-action condenser) and high pressure section condenser 13(be also called purpose double-action condenser), solution pump includes single-action solution pump 33 and economic benefits and social benefits solution pump 34, and solution heat exchanger includes single-action heat exchanger 37, low temperature heat exchanger 4 and high-temperature heat exchanger 6；Waste heat smoke outlet tube 9 is provided with smoke solution heat exchanger 48.This unit energy utilizes high-temperature residual heat flue gas that external device (ED) discharges and afterheat hot water (being also called thermal source hot water) to drive refrigerating operaton simultaneously, refrigeration and heating operation is driven individually with high-temperature residual heat flue gas, it is mainly used in the Distribution of Natural formula energy supplying system of thermal source hot water backwater's temperature very low (being generally below 80 DEG C), waste heat smog discharge temperature can be reduced to less than 120 DEG C when running by refrigeration (heat), and flue gas heat recovery rate is higher.But there is the weak point that solution heat exchanger arrangement components is more and solution circulation pipeline is more complicated in this unit.
Summary of the invention
The purpose of this utility model is in that to overcome above-mentioned deficiency, it is provided that a kind of solution heat exchanger arrangement components is less, simplify the two-period form fume hot-water type lithium bromide absorption refrigerating set of solution circulation pipeline.
nullThe purpose of this utility model is achieved in that a kind of two-period form fume hot-water type lithium-bromide absorption-type refrigerating machine with flue gas heat-exchange unit，Including high tension generator、Vaporizer、Absorber、Steam generator、Hot water generator、Condenser、Smoke solution heat exchanger、High-temperature heat exchanger、Low temperature heat exchanger and solution pump，Vaporizer includes low pressure stage vaporizer and high pressure section vaporizer，Absorber includes low pressure stage absorber and high pressure section absorber，Condenser includes low pressure stage condenser and high pressure section condenser，It is characterized in that: by low pressure stage vaporizer、Low pressure stage absorber and high pressure section vaporizer、High pressure section absorber is arranged in same evaporation absorber cylinder，Low pressure stage vaporizer、Low pressure stage absorber and high pressure section vaporizer、Segmentation dividing plate is inhaled in the steaming being provided with lateral arrangement between high pressure section absorber，Steam to inhale and segmentation dividing plate is provided with cloth liquid bath；Steam generator, high pressure section condenser and hot water generator, low pressure stage condenser are arranged in same generation condenser cylinder, between steam generator, high pressure section condenser and hot water generator, low pressure stage condenser, are provided with generation condenser segmentation dividing plate；The weak solution drain pipe of described low temperature heat exchanger is received on smoke solution heat exchanger as flue gas heat-exchange unit feed tube, flue gas heat-exchange unit drain pipe is received on hot water generator as hot water generator feed tube, going out the solution of hot water generator by solution elevating transport pump, high-temperature heat exchanger received by solution elevating delivery side of pump pipe.
A kind of two-period form fume hot-water type lithium-bromide absorption-type refrigerating machine with flue gas heat-exchange unit of this utility model, the generation condenser segmentation dividing plate between steam generator, high pressure section condenser and hot water generator, low pressure stage condenser is vertically arranged.
A kind of two-period form fume hot-water type lithium-bromide absorption-type refrigerating machine with flue gas heat-exchange unit of this utility model, the generation condenser segmentation dividing plate lateral arrangement between steam generator, high pressure section condenser and hot water generator, low pressure stage condenser.
A kind of two-period form fume hot-water type lithium-bromide absorption-type refrigerating machine with flue gas heat-exchange unit of this utility model, described high tension generator is flue gas type high tension generator.
A kind of two-period form fume hot-water type lithium-bromide absorption-type refrigerating machine with flue gas heat-exchange unit of this utility model, described high tension generator includes flue gas type high tension generator and Direct Fired High Pressure Generator, and the drain pipe occurred frequently of flue gas type high tension generator is accessed Direct Fired High Pressure Generator.
A kind of two-period form fume hot-water type lithium-bromide absorption-type refrigerating machine with flue gas heat-exchange unit of this utility model, described high tension generator is integral type fuel supplementing type high tension generator.
The beneficial effects of the utility model are:
This utility model arranges the steaming of lateral arrangement in the evaporation absorber cylinder of unit and inhales segmentation dividing plate, makes evaporation absorber become the two-period form structure of upper and lower segmentation；In there is condenser cylinder, it is provided with generation condenser segmentation dividing plate, makes generation condenser become two-period form structure.Cancel single-action heat exchanger, simplify solution circulation pipeline.During unit refrigerating operaton, lithium-bromide solution can complete the conveying needed for single dual-effect refrigeration cycle of operation through following parts, heat exchange, heating concentration and absorption dilution, without single-action heat exchanger: solution pump (conveying) → low temperature heat exchanger (heat exchange intensification) → hot water generator (heating concentration) → solution elevating pump (conveying) → smoke solution heat exchanger (heat exchange intensification) → high-temperature heat exchanger (heat exchange intensification) → high tension generator (heating concentration) → high-temperature heat exchanger (heat exchange cooling) → steam generator (heating concentration) → low temperature heat exchanger (heat exchange cooling) → low pressure stage absorber (absorbing dilution) → high pressure section absorber (absorbing dilution).
Accompanying drawing explanation
Fig. 1 is the conventional two-period form fume hot-water type lithium-bromide absorption-type refrigerating machine structural representation with flue gas heat-exchange unit.
Fig. 2 is this utility model two-period form fume hot-water type lithium-bromide absorption-type refrigerating machine with flue gas heat-exchange unit.
Fig. 3 is this utility model two-period form fume hot-water type lithium-bromide absorption-type refrigerating machine structural representation with flue gas heat-exchange unit, and the generation condenser segmentation dividing plate between steam generator, high pressure section condenser and hot water generator, low pressure stage condenser adopts lateral arrangement.
Fig. 4 is this utility model two-period form fume hot-water type lithium-bromide absorption-type refrigerating machine structural representation with flue gas heat-exchange unit, and fuel supplementing type high tension generator is split type afterburning structure.
Fig. 5 is this utility model two-period form fume hot-water type lithium-bromide absorption-type refrigerating machine structural representation with flue gas heat-exchange unit, and fuel supplementing type high tension generator is integral type afterburning structure.
Accompanying drawing labelling in figure:
nullHigh pressure section vaporizer 1、High pressure section absorber 2、Solution switching valve 3、Low temperature heat exchanger 4、Solution elevating pump 5、High-temperature heat exchanger 6、Drain pipe 7 occurred frequently、Flue gas type high tension generator 8、Waste heat smoke outlet tube 9、Waste heat flue gas inlet tube 10、Steam switching valve 11、Refrigerant vapour pipe 12、High pressure section condenser 13、Steam generator 14、Hot water generator 15、Thermal source hot water outlet pipe 16、Low pressure stage condenser 17、Thermal source hot water inlet pipe 18、Low pressure stage absorber 19、Cooling water outlet pipe 20、Low pressure stage vaporizer 21、Cold (heat) water outlet pipe 22、Steam contracture section dividing plate 23、Cold (heat) water inlet pipe 24、Evaporation absorber cylinder 25、Solution pump 26、Cryogenic fluid pump 27、Cooling water inlet pipe 28、Steam generator feed tube 29、Hot water generator feed tube 30、Single effect absorption device 31、Single effect evaporator 32、Single-action solution pump 33、Economic benefits and social benefits solution pump 34、Double effect evaporator 35、Double-effect absorption device 36、Single-action heat exchanger 37、Burner 38、Direct Fired High Pressure Generator 39、Afterburning smoke outlet tube 40、Integral type fuel supplementing type high tension generator 41、Cloth liquid bath 42、Cloth tank 43、There is condenser segmentation dividing plate 44、There is condenser cylinder 45、Flue gas heat-exchange unit feed tube 46、Flue gas heat-exchange unit drain pipe 47、Smoke solution heat exchanger 48、Waste heat smoke discharge pipe 49.
Detailed description of the invention
This utility model is unit as shown in Figure 2, this unit be by flue gas type high tension generator 8, vaporizer, absorber, steam generator 14, hot water generator 15, condenser, smoke solution heat exchanger 48, high-temperature heat exchanger 6, low temperature heat exchanger 4, solution pump 26, solution elevating pump 5, cryogenic fluid pump 27, control system (not shown) and the pipeline of connecting components, the two-period form flue gas pattern of fever cold/hot water machine of lithium bromide group with flue gas heat-exchange unit that valve is constituted.Vaporizer includes low pressure stage vaporizer 21 and high pressure section vaporizer 1, and absorber includes low pressure stage absorber 19 and high pressure section absorber 2, and condenser includes low pressure stage condenser 17 and high pressure section condenser 13；Low pressure stage vaporizer 21, low pressure stage absorber 19 and high pressure section vaporizer 1, high pressure section absorber 2 are arranged in same evaporation absorber cylinder 25, segmentation dividing plate 23 is inhaled in the steaming being provided with lateral arrangement between low pressure stage vaporizer 21, low pressure stage absorber 19 and high pressure section vaporizer 1, high pressure section absorber 2, make two-period form evaporation absorber become upper and lower segmental structure to arrange, steam and suction segmentation dividing plate 23 is provided with cloth liquid bath 42 and cloth tank 43；Steam generator 14, high pressure section condenser 13 and hot water generator 15, low pressure stage condenser 17 are arranged in same generation condenser cylinder 45, it is provided with the generation condenser segmentation dividing plate 44 being vertically arranged between steam generator 14, high pressure section condenser 13 and hot water generator 15, low pressure stage condenser 17, makes two-period form generation condenser become left and right segmental structure and arrange；The weak solution drain pipe of low temperature heat exchanger 4 is received on smoke solution heat exchanger 48 as flue gas heat-exchange unit feed liquor 46, and flue gas heat-exchange unit drain pipe 47 is received on hot water generator 15 as hot water generator feed tube 30.The intermediate solution drain pipe of high-temperature heat exchanger 6 is received on steam generator 14 as steam generator feed tube 29.The solution going out hot water generator 15 is carried by solution elevating pump 5, and the outlet of solution elevating pump 5 is received on high-temperature heat exchanger 6.Connecting line between drain pipe 7 occurred frequently and evaporation absorber cylinder 25 switches valve 3 equipped with solution；Connecting line between refrigerant vapour pipe 12 and evaporation absorber cylinder 25 switches valve 11 equipped with steam.
When unit utilizes waste heat flue gas and thermal source hot water heating refrigerating operaton simultaneously, solution switching valve 3 and steam switching valve 11 are closed.The weak solution going out high pressure section absorber 2 is carried by solution pump 26, is entered hot water generator 15 through hot water generator feed tube 30 after low temperature heat exchanger 4 heat exchange heats up, and is concentrated by the thermal source hot water heating from external device (ED)s such as gas engines；The solution going out hot water generator 15 is carried by solution elevating pump 5, is entered smoke solution heat exchanger 48 heat exchange intensification through flue gas heat-exchange unit feed tube 46, then enter entrance flue gas type high tension generator 8 after high-temperature heat exchanger 6 heat exchange heats up through flue gas heat-exchange unit drain pipe 47, is condensed into intermediate solution by the high-temperature residual heat flue gas from external device (ED)s such as gas engines further；The intermediate solution going out flue gas type high tension generator 8 enters steam generator 14 through steam generator feed tube 29 after high-temperature heat exchanger 6 heat exchange is lowered the temperature, and is heated further and is condensed into concentrated solution；Concentrated solution goes out steam generator 14, enters low pressure stage absorber 19 after low temperature heat exchanger 4 heat exchange is lowered the temperature, low pressure stage absorber 19 absorb from the water vapour in low pressure stage vaporizer 21, concentration imports after reducing steams in the cloth liquid bath 42 inhaled on segmentation dividing plate 23, and enter high pressure section absorber 2 from the liquid distributing hole bottom cloth liquid bath 42, absorb further from the water vapour in high pressure section vaporizer 1, concentration reduces further and becomes weak solution, thus completing a heat exchange, concentration occurring and absorbs single dual-effect refrigeration cycle of operation of dilution.
During unit heat supply running, solution switching valve 3 and steam switching valve 11 are opened, cryogenic fluid pump 27 stall.The weak solution going out high pressure section absorber 2 is carried by solution pump 26, hot water generator 15 is entered through low temperature heat exchanger 4 and hot water generator feed tube 30, then go out hot water generator 15, solution elevating pump 5 carry, enter smoke solution heat exchanger 48 heat exchange intensification through flue gas heat-exchange unit feed tube 46, then enter flue gas type high tension generator 8 through flue gas heat-exchange unit drain pipe 47 and high-temperature heat exchanger 6, be condensed into concentrated solution by the high-temperature residual heat flue gas from external device (ED)s such as gas engines；The concentrated solution going out flue gas type high tension generator 8 enters low pressure stage absorber 19 through solution switching valve 3, then import and steam in the cloth liquid bath 42 inhaled on segmentation dividing plate 23, and enter high pressure section absorber 2 from the liquid distributing hole bottom cloth liquid bath 42, be mixed into weak solution with from the water as refrigerant in high pressure section vaporizer 1, thus complete one occur concentration and mixed diluting heat cycle of operation.
Transversal sectional is adopted to arrange on the generation condenser segmentation dividing plate 44 in the condenser cylinder of unit generation shown in Fig. 2 45, making two-period form generation condenser become upper and lower segmental structure, namely this unit becomes the two-period form fume hot-water type cold/hot water machine of lithium bromide group shown in Fig. 3 with flue gas heat-exchange unit.
Unit shown in Fig. 2 is set up Direct Fired High Pressure Generator 39, and the drain pipe occurred frequently 7 of flue gas type high tension generator 8 is accessed Direct Fired High Pressure Generator 39, namely this unit becomes the two-period form fume hot-water fuel supplementing type cold/hot water machine of lithium bromide group shown in Fig. 4 with flue gas heat-exchange unit.
With the flue gas type high tension generator 8 in unit shown in integral type fuel supplementing type high tension generator 41 alternate figures 2, namely this unit becomes the two-period form fume hot-water fuel supplementing type cold/hot water machine of lithium bromide group shown in Fig. 5 with flue gas heat-exchange unit.
Cancelling the solution switching valve 3 in unit shown in Fig. 2～Fig. 5, steam switching valve 11 and connecting tube thereof, namely unit becomes for separate refrigeration, two-period form fume hot-water (afterburning) type lithium bromide adsorption water chilling unit with flue gas heat-exchange unit.
Claims (6)
- null1. the two-period form fume hot-water type lithium-bromide absorption-type refrigerating machine with flue gas heat-exchange unit，Including high tension generator、Vaporizer、Absorber、Steam generator (14)、Hot water generator (15)、Condenser、Smoke solution heat exchanger (48)、High-temperature heat exchanger (6)、Low temperature heat exchanger (4) and solution pump (26)，Vaporizer includes low pressure stage vaporizer (21) and high pressure section vaporizer (1)，Absorber includes low pressure stage absorber (19) and high pressure section absorber (2)，Condenser includes low pressure stage condenser (17) and high pressure section condenser (13)，It is characterized in that: by low pressure stage vaporizer (21)、Low pressure stage absorber (19) and high pressure section vaporizer (1)、High pressure section absorber (2) is arranged in same evaporation absorber cylinder (25)，Low pressure stage vaporizer (21)、Low pressure stage absorber (19) and high pressure section vaporizer (1)、Segmentation dividing plate (23) is inhaled in the steaming being provided with lateral arrangement between high pressure section absorber (2)，Steam to inhale and segmentation dividing plate (23) is provided with cloth liquid bath (42、43)；Steam generator (14), high pressure section condenser (13) and hot water generator (15), low pressure stage condenser (17) are arranged in same generation condenser cylinder (45), between steam generator (14), high pressure section condenser (13) and hot water generator (15), low pressure stage condenser (17), are provided with generation condenser segmentation dividing plate (44)；The weak solution drain pipe of described low temperature heat exchanger (4) is received on smoke solution heat exchanger (48) as flue gas heat-exchange unit feed tube (46), and flue gas heat-exchange unit drain pipe (47) is received on hot water generator (15) as hot water generator feed tube (30)；The solution going out hot water generator (15) is carried by solution elevating pump (5), and high-temperature heat exchanger (6) received by the outlet of solution elevating pump (5).
- 2. a kind of two-period form fume hot-water type lithium-bromide absorption-type refrigerating machine with flue gas heat-exchange unit according to claim 1, it is characterised in that: generation condenser segmentation dividing plate (44) between steam generator (14), high pressure section condenser (13) and hot water generator (15), low pressure stage condenser (17) is vertically arranged.
- 3. a kind of two-period form fume hot-water type lithium-bromide absorption-type refrigerating machine with flue gas heat-exchange unit according to claim 1, it is characterised in that: generation condenser segmentation dividing plate (44) lateral arrangement between steam generator (14), high pressure section condenser (13) and hot water generator (15), low pressure stage condenser (17).
- 4. a kind of two-period form fume hot-water type lithium-bromide absorption-type refrigerating machine with flue gas heat-exchange unit according to claim 1 or 2 or 3, it is characterised in that: described high tension generator is flue gas type high tension generator (8).
- 5. a kind of two-period form fume hot-water type lithium-bromide absorption-type refrigerating machine with flue gas heat-exchange unit according to claim 1 or 2 or 3, it is characterized in that: described high tension generator includes flue gas type high tension generator (8) and Direct Fired High Pressure Generator (39), and the drain pipe occurred frequently (7) of flue gas type high tension generator (8) is accessed Direct Fired High Pressure Generator (39).
- 6. a kind of two-period form fume hot-water type lithium-bromide absorption-type refrigerating machine with flue gas heat-exchange unit according to claim 1 or 2 or 3, it is characterised in that: described high tension generator is integral type fuel supplementing type high tension generator (41).
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620153927.3U CN205403238U (en) | 2016-03-01 | 2016-03-01 | Take gas gas heater's two -period form flue gas hot water type lithium bromide absorbed refrigeration machine |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620153927.3U CN205403238U (en) | 2016-03-01 | 2016-03-01 | Take gas gas heater's two -period form flue gas hot water type lithium bromide absorbed refrigeration machine |
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| CN205403238U true CN205403238U (en) | 2016-07-27 |
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| CN201620153927.3U Active CN205403238U (en) | 2016-03-01 | 2016-03-01 | Take gas gas heater's two -period form flue gas hot water type lithium bromide absorbed refrigeration machine |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105650928A (en) * | 2016-03-01 | 2016-06-08 | 双良节能系统股份有限公司 | Two-section type smoke hot water type lithium bromide absorption type refrigerator with smoke heat exchanger |
| CN106225324A (en) * | 2016-09-13 | 2016-12-14 | 远大空调有限公司 | A kind of absorber liquid distributor and the absorber containing this liquid distributor |
-
2016
- 2016-03-01 CN CN201620153927.3U patent/CN205403238U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105650928A (en) * | 2016-03-01 | 2016-06-08 | 双良节能系统股份有限公司 | Two-section type smoke hot water type lithium bromide absorption type refrigerator with smoke heat exchanger |
| CN106225324A (en) * | 2016-09-13 | 2016-12-14 | 远大空调有限公司 | A kind of absorber liquid distributor and the absorber containing this liquid distributor |
| CN106225324B (en) * | 2016-09-13 | 2018-10-09 | 远大空调有限公司 | A kind of absorber liquid distributor and the absorber containing the liquid distributor |
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