CN202182509U - Combined heat and power heating system with absorbing type refrigeration and heat exchange - Google Patents
Combined heat and power heating system with absorbing type refrigeration and heat exchange Download PDFInfo
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- CN202182509U CN202182509U CN2011202954497U CN201120295449U CN202182509U CN 202182509 U CN202182509 U CN 202182509U CN 2011202954497 U CN2011202954497 U CN 2011202954497U CN 201120295449 U CN201120295449 U CN 201120295449U CN 202182509 U CN202182509 U CN 202182509U
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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
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Abstract
The utility model relates to a combined heat and power heating system with absorbing type refrigeration and heat exchange, comprising an extraction-condensation type steam turbine (1), a steam turbine gas extracting pipe (2), a main condenser (3), a main water heat exchanger (4), an auxiliary condenser (5), an auxiliary water heat exchanger (6), a steam-water heat exchanger (9), a water-water heat exchanger (14), absorbing type heat pumps [XR(1...m) (1...n)] and absorbing type refrigerators (XZ1...p). After entering a thermal power plant, heat supply network return water is divided into two paths: one path of heat supply network return water is subjected to temperature rising by the auxiliary water heat exchanger (6), the absorbing type heat pump absorber, and the condenser, the other path of heat supply network return water is subjected to temperature rising by the condenser (7), the two paths or a plurality of paths of heat supply network return water are combined finally, subjected to temperature rising by the steam-water heat exchanger (9), then are taken as a driving heat source to be sent into the absorbing type refrigerators (XZ1...p) in parallel, are refrigerated, and then are subjected to temperature reducing again by the water-water heat exchanger (14) so as to return to the thermal power plant. The combined heat and power heating system with the absorbing type refrigeration and heat exchange can recover more condensing waste heat of the thermal power plant, the running efficiency of the heat pump can be improved, and the heat supply network can run more reliably.
Description
Technical field
The utility model relates to a kind of cogeneration heating system, is applicable to that the exhaust steam of cogeneration power plant steam turbine is more energy-conservation, utilizes safely and reliably, and heat network system more utilizes condensation waste heat.
Background technology
Along with the shortage of the energy and the requirement of energy-saving and emission-reduction improve day by day, the comprehensive utilization technique of the energy is in continuous lifting.Urban planning cogeneration in the north carries out central heating, to substitute original independent boiler central heating, realizes the requirement of energy-saving and emission-reduction.Make full use of steam power plant's used heat, to improve the heat capacity of steam power plant, realize energy-saving and emission-reduction better, guarantee the safe and reliable operation of steam power plant and heat supply network simultaneously again, various new flow processs require study.Realize the more turbine discharge used heat that reclaims in the power plant, the most important condition is that adopting with the electricity is the source pump of power, or is the absorption type heat pump assembly of power with the heat supply network high-temperature water with the secondary net return water temperature reduction of hot user side.Heat supply network backwater through power plant is confessed carries out refrigeration cool-down, and thermal source supplies the secondary net to use again, makes the heat supply network return water temperature reduce back telegram in reply factory.Power plant heat supply network backwater is introduced into former plant condenser after getting into power plant, with electric power plant circulating water be blended in heat up in the condenser after, get into absorption heat pump again, see off after in heat pump, heating up.In this system, the temperature that recirculated water goes out heat pump is the keys of heat supply network in many recovery of whole heating season condensation heat, in same outlet temperature, can reclaim more condensation waste heat, and become the another difficult problem of steam power plant's central heating technology with high-grade drawing gas less.
Summary of the invention
The purpose of the utility model is to overcome above-mentioned deficiency, and a kind of condensation waste heat of realizing reclaiming more steam power plants is provided, and the operational efficiency of raising heat pump and power plant system heat network system be the absorption refrigeration heat exchange cogeneration heating system of reliability service more.
The purpose of the utility model is achieved in that a kind of absorption refrigeration heat exchange cogeneration heating system; Comprise sucking condensing turbine, extracted steam from turbine pipe, main condenser, auxilliary condenser and vapor-water heat exchanger, high steam is extracted the thermal source of part steam as absorption heat pump and vapor-water heat exchanger out in sucking condensing turbine work done generating back.Main frame, subsidiary engine exhaust steam in steam turbine condense into water by main and auxiliary condenser, and condensation waste heat is recycled.It is characterized in that: in steam power plant, set up the absorption heat pump XR (1 that has subcooler ... M) (1 ... N); In said heating system, have additional main water water-to-water heat exchanger and auxilliary water water-to-water heat exchanger; In heating plant, set up Absorption Refrigerator XZ (1 ... P) and the water water-to-water heat exchanger; M, n and p be >=2 natural number; The heat supply network backwater is divided into two tunnel: one road heat supply network backwater single channel or the parallelly connected absorber that gets into first absorption heat pump of demultiplexing behind auxilliary water water-to-water heat exchanger before getting into auxilliary water water-to-water heat exchanger; Get into the absorber of second absorption heat pump again ... Be connected in series successively; Until getting into the (1 ... M) absorber of n platform absorption heat pump; Go out the condenser that gets into this absorption heat pump behind this absorber again, then from the (1 ... M) (n-1) the, the (1 ... M) (n-2) ... Be connected in series successively, from the condenser of first absorption heat pump, go out at last; The parallel connection of another road heat supply network backwater single channel or demultiplexing gets into the subcooler of each absorption heat pump, the two road or multichannel heat supply network backwater merge at last, after vapor-water heat exchanger is heated, see off again to heating plant; The cooling circulating water of main condenser gets into main water water-to-water heat exchanger, returns main condenser after the heat release, and the evaporimeter of absorption heat pump and main water water-to-water heat exchanger, auxilliary water water-to-water heat exchanger, main condenser, auxilliary condenser are separately or be connected in parallel; The cool cycles water out of auxilliary condenser is connected with auxilliary water water-to-water heat exchanger; Heat supply network hot water is introduced into Absorption Refrigerator as heat power after delivering to user's heating plant, reduces temperature, goes out the laggard entry water-to-water heat exchanger of Absorption Refrigerator;, the water water-to-water heat exchanger returns steam power plant again after reducing temperature; The secondary heat supply network backwater of user's heating plant get into be divided into behind user's heating plant two the tunnel: the one tunnel be introduced into Absorption Refrigerator evaporimeter, got into the water water-to-water heat exchanger behind the refrigeration cool-down again, and heat up after the hot net water heat exchange; Another road secondary hot net water gets into the Absorption Refrigerator heat absorbing side; As cooling water the heat in the refrigeration machine is taken away, the back two tunnel of heating up merges, and is sent to user's heat supply.
The utility model absorption refrigeration heat exchange cogeneration heating system; The circulating water outlet of said main water water-to-water heat exchanger divides be introduced into (1 at two the tunnel: the one tunnel ... M) evaporimeter of n platform absorption heat pump; Return successively then; Get into the evaporimeter of second, first absorption heat pump, from first absorption heat pump, go out at last, return main water water-to-water heat exchanger; Another road gets into the cooling device of steam power plant.
The utility model absorption refrigeration heat exchange cogeneration heating system; The recirculated water of said auxilliary water water-to-water heat exchanger is introduced into the (1 after going out said auxilliary water water-to-water heat exchanger ... M) evaporimeter of n platform absorption heat pump; Return successively then; Get into the evaporimeter of second, first absorption heat pump, from first absorption heat pump, go out at last, return auxilliary water water-to-water heat exchanger.
The utility model absorption refrigeration heat exchange cogeneration heating system; The cool cycles water out of said main condenser is divided into two the tunnel: the one tunnel and is introduced into the (1 ... M) evaporimeter of n platform absorption heat pump; Return successively then, get into the evaporimeter of second, first absorption heat pump, from first absorption heat pump, go out at last; Return main condenser, another Lu Quzhu water water-to-water heat exchanger.
The utility model absorption refrigeration heat exchange cogeneration heating system; The cool cycles water out of said auxilliary condenser is divided into two the tunnel: the one tunnel and is introduced into the (1 ... M) evaporimeter of n platform absorption heat pump; Return successively then, get into the evaporimeter of second, first absorption heat pump, from first absorption heat pump, go out at last; Return auxilliary condenser, auxilliary water water-to-water heat exchanger is removed on another road.
The utility model absorption refrigeration heat exchange cogeneration heating system; The cooling circulating water parallel connection of said main water water-to-water heat exchanger and auxilliary water water-to-water heat exchanger is introduced into the (1 ... M) evaporimeter of n platform absorption heat pump; Return successively then; Get into the evaporimeter of second, first absorption heat pump, from first absorption heat pump, go out at last, main water water-to-water heat exchanger and auxilliary water water-to-water heat exchanger are returned in parallel connection.
The utility model absorption refrigeration heat exchange cogeneration heating system; The cooling circulating water parallel connection of said main condenser and auxilliary condenser is introduced into the (1 ... M) evaporimeter of n platform absorption heat pump; Return successively then; Get into the evaporimeter of second, first absorption heat pump, from first absorption heat pump, go out at last, main condenser and auxilliary condenser are returned in parallel connection.
The utility model absorption refrigeration heat exchange cogeneration heating system, the cooling device of said steam power plant is a cooling tower or a device for cooling.
The utility model absorption refrigeration heat exchange cogeneration heating system; The subcooler of said each absorption heat pump is merged into a subcooler; The water as refrigerant pipeline parallel connection of each absorption heat pump inserts the subcooler after this merging, and subcooler and another road heat supply network backwater that the heat supply network backwater goes out after this merging merge at last.
This absorption refrigeration heat exchange cogeneration heating system also is applicable to an air cooling power plant and a cold power plant.
The beneficial effect of the utility model is:
In steam power plant, setting up has increased each one of main and auxiliary water water-to-water heat exchanger and in heating plant, has set up Absorption Refrigerator and the water water-to-water heat exchanger in the absorption heat pump that has subcooler and the system, the confession heat supply in winter moved when doing heat supply season.Heat supply network recirculated water and power plant's cool cycles water separation isolated operation.Guaranteed the water quality of hot net water, guaranteed that all kinds of heat transmission equipments can safe and reliable energy-efficient operation.Adopt heat supply network recirculated water directly to reclaim the COP value that the heat pump waste heat has more effectively improved heat pump.The working steam of heat pump will be practiced thrift more than 8% than original system.Because heat pump has been used high-grade energy less in reclaiming steam power plant's condensation waste heat process; So compare with former heat pump; Under the situation that reclaims same condensation waste heat; The temperature that goes out heat pump is lower than originally, can guarantee that so more heat supply network reclaims condenser heat and realizes maximization when heating demand descends, and is utilizing more exhaust steam in steam turbine to be used for heating in whole heating season.Because reclaim same condensation heat, the circulating water temperature that goes out heat pump is low, under same outlet temperature situation, the recyclable more condensation waste heat of heat pump.Through heat supply network recirculated water and cooling circulating water corresponding series flow in the absorber of each heat pump and condenser and evaporimeter, make the performance of heat pump obtain better optimize.The volume of heat pump, weight indicator can descend greatly, and manufacturing cost can descend simultaneously.On the other hand, because the performance optimization of heat pump, each item economic technology economic indicator of steam power plant is further enhanced.Increased Absorption Refrigerator at user's heating plant; Through with behind the water-heating cooling of user network with total heat supply network heat exchange; The temperature of total heat supply network backwater is reduced, reclaim low-temperature heat source with auxilliary water water-to-water heat exchanger waste heat heat exchange after the hot net water backheat power plant, increased the yield of waste heat.
Description of drawings
Fig. 1 is connected sketch map for the evaporator with heat pump recirculated water that the utility model relates to main water water-to-water heat exchanger.
Fig. 2 is connected sketch map for the evaporator with heat pump recirculated water that the utility model relates to auxilliary water water-to-water heat exchanger.
Fig. 3 is connected sketch map for the evaporator with heat pump recirculated water that the utility model relates to main condenser.
Fig. 4 is connected sketch map for the evaporator with heat pump recirculated water that the utility model relates to auxilliary condenser.
Fig. 5 is connected sketch map for the evaporator with heat pump recirculated water that the utility model relates to main and auxiliary water water-to-water heat exchanger.
Fig. 6 is connected sketch map for the evaporator with heat pump recirculated water that the utility model relates to main and auxiliary condenser.
Reference numeral among the figure:
Sucking condensing turbine 1, main steam turbine extraction steam pipe 2, main condenser 3, main water water-to-water heat exchanger 4, auxilliary condenser 5, auxilliary water water-to-water heat exchanger 6, subcooler 7, cooling device 8, vapor-water heat exchanger 9, heat supply network return branch 10, heat supply network return branch 11, heat supply network feed pipe 12, heat supply network return pipe 13, water water-to-water heat exchanger 14, secondary heat supply network return pipe 15, secondary heat supply network feed pipe 16, absorption heat pump XR (1 ... M) (1 ... N), Absorption Refrigerator XZ (1 ... P).
The specific embodiment
Below in conjunction with accompanying drawing the utility model is described further:
Embodiment 1:
As shown in Figure 1, Fig. 1 is connected sketch map for the evaporator with heat pump recirculated water that the utility model relates to main water water-to-water heat exchanger.Can find out by Fig. 1; The utility model absorption refrigeration heat exchange cogeneration heating system is by sucking condensing turbine 1, main steam turbine extraction steam pipe 2, main condenser 3, main water water-to-water heat exchanger 4, auxilliary condenser 5, auxilliary water water-to-water heat exchanger 6, subcooler 7, cooling device 8, vapor-water heat exchanger 9, heat supply network return branch 10, heat supply network return branch 11, heat supply network feed pipe 12, heat supply network return pipe 13, water water-to-water heat exchanger 14, secondary heat supply network return pipe 15, secondary heat supply network feed pipe 16, absorption heat pump XR (1 ... M) (1 ... N), Absorption Refrigerator XZ1 ... Compositions such as p and water pump, valve and connecting line.Said absorption heat pump XR has m * n platform, and Absorption Refrigerator XZ has the p platform, and m, n and p be >=2 natural number.The heat supply network backwater is divided into the auxilliary water water-to-water heat exchanger 6 of two tunnel: one road heat supply network backwater access after getting into steam power plant; Go out to assist water water-to-water heat exchanger 6 back single channel or demultiplexing and get into first absorption heat pump XR (1 through 10 parallel connections of heat supply network return branch ... M) 1 absorber; Go out first absorption heat pump XR (1 ... M) get into second absorption heat pump XR (1 behind 1 the absorber ... M) 2 absorber, all the other and the like ... Go out the (1 ... M) (n-1) get into the (1 again behind the absorber of platform absorption heat pump ... M) n platform absorption heat pump XR (1 ... M) absorber of n; Get into the condenser of this heat pump again, get into the (1 then ... M) (n-1) condenser of platform absorption heat pump, all the other and the like;, after first absorption heat pump XR (1 ... M) 1 condenser goes out.This road heat supply network backwater is heated through auxilliary water water-to-water heat exchanger 6; Pass through first absorption heat pump XR (1 of single channel or multichannel again ... M) 1, second absorption heat pump XR (1 ... M) 2 ... The (1 ... M) n platform absorption heat pump XR (1 ... M) absorber of n adds the gentle the (1 ... M) n platform absorption heat pump XR (1 ... M) n ... Second absorption heat pump XR (1 ... M) 2, first absorption heat pump XR (1 ... M) 1 condenser is heated, and the heat supply network return water temperature is raise; Another road heat supply network backwater inserts the subcooler 7 of each absorption heat pump through heat supply network return branch 11 single channel or demultiplexing parallel connection.Heat exchange heats up in subcooler 7, has taken away the heat of absorption heat pump condensation water as refrigerant, and the heat of the water as refrigerant that the heat pump generator produces has obtained effective utilization.Two the road or multichannel heat supply network backwater merge at last, after vapor-water heat exchanger 9 heats up, see off again by heat supply network feed pipe 12.Because water as refrigerant cooling back gets into evaporimeter; Basically eliminated the liquid state loss that water as refrigerant gets into behind the evaporimeter self flash distillation cooling; Make water as refrigerant can all be used for refrigeration, the COP value of heat pump is improved, reached the effect that one action two gets cooling circulating water.The cooling circulating water of the main condenser 3 of steam power plant gets into main water water-to-water heat exchanger 4, heats to return main condenser 3 behind the main water water-to-water heat exchanger 4 opposite side recirculated waters and heat.The recirculated water of main water water-to-water heat exchanger 4 is divided into two the tunnel: the one tunnel and is introduced into the (1 ... M) n platform absorption heat pump XR (1 ... M) evaporimeter of n; Return successively then; Get into second absorption heat pump XR (1 ... M) 2, first absorption heat pump XR (1 ... M) 1 evaporimeter is at last from first absorption heat pump XR (1 ... M) returning main water water-to-water heat exchanger 4 after 1 evaporimeter flows out heats again; Another road enters atmosphere to unnecessary heat through cooling device 8.The cooling circulating water of auxilliary condenser 5 gets into auxilliary water water-to-water heat exchanger 6, returns auxilliary condenser 5 behind the heating heat supply network backwater and heats.Circulating water line in the absorption heat pump evaporimeter also can with auxilliary water water-to-water heat exchanger 6, main condenser 3 and auxilliary condenser 5 separately or be connected in parallel.
The high temperature heat supply network supplies water and inserts Absorption Refrigerator XZ (1 through 12 parallel connections of heat supply network feed pipe in the heating plant ... P) as driving heat source; Reduce temperature; Go out Absorption Refrigerator XZ (1 ... P) laggard entry water-to-water heat exchanger 14 returns steam power plant by heat supply network return pipe 13 after water water-to-water heat exchanger 14 reduces temperature once more.The secondary heat supply network backwater of heating plant is divided into two the tunnel: the one tunnel and gets into Absorption Refrigerator XZ (1 after secondary heat supply network return pipe 15 gets into heating plant ... P) evaporimeter is heated up after laggard entry water-to-water heat exchanger 14 of refrigeration cool-down and the hot net water heat exchange; Another road gets into Absorption Refrigerator XZ (1 ... P) heat absorbing side is taken away the heat in the refrigeration machine as cooling water, heats up back two tunnel hydrations also, is sent to user's heat supply by secondary heat supply network feed pipe 16.
In this system heat supply network recirculated water and cooling circulating water two at the most the series flow in the platform heat pump make the performance of heat pump obtain optimization, each item technical-economic index of power plant's cogeneration operation is further improved.
Described heat supply network backwater also can carry out heat exchange with a shared subcooler (not drawing among the figure) of many heat pumps.The water as refrigerant pipeline of each heat pump (not drawing among the figure) is connected in parallel with subcooler, through backheat pump after the subcooler heat release.After heating up in subcooler, the heat supply network backwater merges with another road.
Embodiment 2:
As shown in Figure 2, Fig. 2 is connected sketch map for the evaporator with heat pump recirculated water that the utility model relates to auxilliary water water-to-water heat exchanger.The main difference of Fig. 2 and Fig. 1 is absorption heat pump XR (1 ... M) (1 ... N) evaporimeter recirculated water is connected with auxilliary water water-to-water heat exchanger 6.
Embodiment 3:
As shown in Figure 3, Fig. 3 is connected sketch map for the evaporator with heat pump recirculated water that the utility model relates to main condenser.The main difference of Fig. 3 and Fig. 1 is absorption heat pump XR (1 ... M) (1 ... N) evaporimeter recirculated water is connected with main condenser 3.
Embodiment 4:
As shown in Figure 4, Fig. 4 is connected sketch map for the evaporator with heat pump recirculated water that the utility model relates to auxilliary condenser.The main difference of Fig. 4 and Fig. 1 is absorption heat pump XR (1 ... M) (1 ... N) evaporimeter recirculated water is connected with auxilliary condenser 5.
Embodiment 5:
As shown in Figure 5, Fig. 5 is connected sketch map for the evaporator with heat pump recirculated water that the utility model relates to main and auxiliary water water-to-water heat exchanger.The main difference of Fig. 5 and Fig. 1 is absorption heat pump XR (1 ... M) (1 ... N) evaporimeter recirculated water is connected with auxilliary water water-to-water heat exchanger 6 with main water water-to-water heat exchanger 4.
Embodiment 6:
As shown in Figure 6, Fig. 6 is connected sketch map for the evaporator with heat pump recirculated water that the utility model relates to main and auxiliary condenser.The main difference of Fig. 6 and Fig. 1 is absorption heat pump XR (1 ... M) (1 ... N) evaporimeter recirculated water is connected with auxilliary condenser 5 with main condenser 3.
Claims (9)
1. absorption refrigeration heat exchange cogeneration heating system; Comprise sucking condensing turbine (1), extracted steam from turbine pipe (2), main condenser (3), auxilliary condenser (5) and vapor-water heat exchanger (9), it is characterized in that: { XR (1 in steam power plant, to set up the absorption heat pump that has subcooler (7) ... M) (1 ... N) }; In said heating system, have additional main water water-to-water heat exchanger (4) and auxilliary water water-to-water heat exchanger (6); In heating plant, set up Absorption Refrigerator (XZ1 ... P) and water water-to-water heat exchanger (14); Said m, n and p be >=2 natural number; The heat supply network backwater gets into that auxilliary water water-to-water heat exchanger (6) is preceding to be divided into two tunnel: one road heat supply network backwater { XR (1 through auxilliary water water-to-water heat exchanger (6) back single channel or first absorption heat pump of the parallelly connected entering of demultiplexing ... M) absorber of 1}; { XR (1 to get into second absorption heat pump again ... M) absorber of 2} ... Be connected in series successively; Until getting into the (1 ... M) { XR (1 for n platform absorption heat pump ... M) absorber of n}; Go out to get into this absorption heat pump again behind this absorber { XR (1 ... M) condenser of n} is then from the (1 ... M) (n-1) the, the (1 ... M) (n-2) ... Be connected in series successively, { XR (1 from first absorption heat pump at last ... M) go out in the condenser of 1}; Another road heat supply network backwater single channel or demultiplexing parallel connection get into the subcooler (7) of each absorption heat pump; Two the road or multichannel heat supply network backwater merge at last; Behind vapor-water heat exchanger (9), see off again to heating plant; The cooling circulating water of main condenser (3) returns main condenser (3) after getting into main water water-to-water heat exchanger (4); { XR (1 for absorption heat pump ... M) evaporimeter of n} and main water water-to-water heat exchanger (4), auxilliary water water-to-water heat exchanger (6), main condenser (3), auxilliary condenser (5) separately or be connected in parallel, the cool cycles water out of auxilliary condenser (5) is connected with auxilliary water water-to-water heat exchanger (6), heat supply network hot water is introduced into Absorption Refrigerator (XZ1 after delivering to user's heating plant ... P); Go out Absorption Refrigerator (XZ1 ... P) laggard entry water-to-water heat exchanger (14); Return steam power plant again, be divided into two the tunnel: the one tunnel behind the secondary heat supply network backwater entering user heating plant of user's heating plant and be introduced into Absorption Refrigerator (XZ1 ... P) evaporimeter gets into water water-to-water heat exchanger (14) again; Another road secondary hot net water gets into Absorption Refrigerator (XZ1 ... P) heat absorbing side, two road secondary hot net waters merge.
2. a kind of absorption refrigeration heat exchange cogeneration heating system according to claim 1; It is characterized in that: the circulating water outlet of said main water water-to-water heat exchanger (4) divides be introduced into (1 at two the tunnel: the one tunnel ... M) { XR (1 for n platform absorption heat pump ... M) evaporimeter of n}; Return successively then; Get into the evaporimeter of second, first absorption heat pump, { XR (1 from first absorption heat pump at last ... M) go out among the 1}, return main water water-to-water heat exchanger (4); Another road gets into the cooling device (8) of steam power plant.
3. a kind of absorption refrigeration heat exchange cogeneration heating system according to claim 1; It is characterized in that: the recirculated water of said auxilliary water water-to-water heat exchanger (6) is introduced into the (1 after going out said auxilliary water water-to-water heat exchanger (6) ... M) { XR (1 for n platform absorption heat pump ... M) evaporimeter of n}; Return successively then; Get into the evaporimeter of second, first absorption heat pump, { XR (1 from first absorption heat pump at last ... M) go out among the 1}, return auxilliary water water-to-water heat exchanger (6).
4. a kind of absorption refrigeration heat exchange cogeneration heating system according to claim 1; It is characterized in that: the cool cycles water out of said main condenser (3) is divided into two the tunnel: the one tunnel and is introduced into the (1 ... M) { XR (1 for n platform absorption heat pump ... M) evaporimeter of n}; Return successively then, get into the evaporimeter of second, first absorption heat pump, { XR (1 from first absorption heat pump at last ... M) go out among the 1}; Return main condenser (3), another Lu Quzhu water water-to-water heat exchanger (4).
5. a kind of absorption refrigeration heat exchange cogeneration heating system according to claim 1; It is characterized in that: the cool cycles water out of said auxilliary condenser (5) is divided into two the tunnel: the one tunnel and is introduced into the (1 ... M) { XR (1 for n platform absorption heat pump ... M) evaporimeter of n}; Return successively then, get into the evaporimeter of second, first absorption heat pump, { XR (1 from first absorption heat pump at last ... M) go out among the 1}; Return auxilliary condenser (5), auxilliary water water-to-water heat exchanger (6) is removed on another road.
6. a kind of absorption refrigeration heat exchange cogeneration heating system according to claim 1; It is characterized in that: the cooling circulating water parallel connection of said main water water-to-water heat exchanger (4) and auxilliary water water-to-water heat exchanger (6) is introduced into the (1 ... M) { XR (1 for n platform absorption heat pump ... M) evaporimeter of n}; Return successively then; Get into the evaporimeter of second, first absorption heat pump; { XR (1 from first absorption heat pump at last ... M) go out among the 1}, main water water-to-water heat exchanger (4) and auxilliary water water-to-water heat exchanger (6) are returned in parallel connection.
7. a kind of absorption refrigeration heat exchange cogeneration heating system according to claim 1; It is characterized in that: the cooling circulating water parallel connection of said main condenser (3) and auxilliary condenser (5) is introduced into the (1 ... M) { XR (1 for n platform absorption heat pump ... M) evaporimeter of n}; Return successively then; Get into the evaporimeter of second, first absorption heat pump, { XR (1 from first absorption heat pump at last ... M) go out among the 1}, main condenser (3) and auxilliary condenser (5) are returned in parallel connection.
8. a kind of absorption refrigeration heat exchange cogeneration heating system according to claim 2, it is characterized in that: the cooling device of said steam power plant (8) is a cooling tower or a device for cooling.
9. according to one of them described a kind of absorption refrigeration heat exchange cogeneration heating system of claim 1 ~ 8; It is characterized in that: the subcooler of said each absorption heat pump (7) is merged into a subcooler; The water as refrigerant pipeline parallel connection of each absorption heat pump inserts the subcooler after this merging, and subcooler and another road heat supply network backwater that the heat supply network backwater goes out after this merging merge at last.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011202954497U CN202182509U (en) | 2011-08-13 | 2011-08-13 | Combined heat and power heating system with absorbing type refrigeration and heat exchange |
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| CN2011202954497U CN202182509U (en) | 2011-08-13 | 2011-08-13 | Combined heat and power heating system with absorbing type refrigeration and heat exchange |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102384515A (en) * | 2011-08-13 | 2012-03-21 | 双良节能系统股份有限公司 | Absorption type refrigeration and heat exchange heat and power cogeneration heating system |
| CN105737236A (en) * | 2016-03-16 | 2016-07-06 | 北京建筑大学 | Two-grade evaporation efficiency improvement type jet heat exchanger unit and application |
-
2011
- 2011-08-13 CN CN2011202954497U patent/CN202182509U/en not_active Withdrawn - After Issue
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102384515A (en) * | 2011-08-13 | 2012-03-21 | 双良节能系统股份有限公司 | Absorption type refrigeration and heat exchange heat and power cogeneration heating system |
| CN102384515B (en) * | 2011-08-13 | 2013-08-07 | 双良节能系统股份有限公司 | Absorption type refrigeration and heat exchange heat and power cogeneration heating system |
| CN105737236A (en) * | 2016-03-16 | 2016-07-06 | 北京建筑大学 | Two-grade evaporation efficiency improvement type jet heat exchanger unit and application |
| CN105737236B (en) * | 2016-03-16 | 2019-03-19 | 北京建筑大学 | A kind of double flash evaporation Synergistic type jetting type heat exchange unit and application |
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