CN100504242C - Two-stage and multi-stage first kind absorption heat pump - Google Patents
Two-stage and multi-stage first kind absorption heat pump Download PDFInfo
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- CN100504242C CN100504242C CNB2006100704289A CN200610070428A CN100504242C CN 100504242 C CN100504242 C CN 100504242C CN B2006100704289 A CNB2006100704289 A CN B2006100704289A CN 200610070428 A CN200610070428 A CN 200610070428A CN 100504242 C CN100504242 C CN 100504242C
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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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Abstract
The invention provides a two-stage/multistage first-type adsorption heat pump, substantially formed by an evaporator, an adsorption-evaporator, an absorber, a generator, a condenser, a throttle valve, a solution pump, and a solution heat exchanger. The coolant steam of generator is fed into the condenser and condensed into liquid, via the throttle valve to be fed into the evaporator and the adsorption-evaporator, or via the throttle valve to be fed into the evaporator to be gasified partly, while the not gasified coolant liquid via the pressurizing pump is fed into the adsorption-evaporator; the coolant steam of evaporator is fed into the first-stage adsorption-evaporator to be absorbed by the solution and release heat, to heat the coolant liquid that fed into the first-stage adsorption evaporator via another branch, to gasify the coolant liquid into high-temperature coolant steam to be fed into the absorber or next-stage adsorption-evaporator, to improve the temperature; and the dilute solution of first-stage adsorption-evaporator is pumped into the generator to heat the coolant steam, then to be fed into the inlet-outlet absorbers, the adsorption evaporators to absorb the coolant steam; the heated liquid flows the inlet-outlet absorbers and the condensers to absorb heat. The invention has simple structure, while it can improve temperature via at least two stages.
Description
Technical field:
The invention belongs to low temperature exhaust heat and utilize technical field of heat pumps.
Background technology:
Adopting the absorption heat pump technology to carry out UTILIZATION OF VESIDUAL HEAT IN is effective means, has reasonable energy-saving and environmental protection and economic benefit, and the prerequisite of utilizing heat pump is that heat pump can rise to heat more than the level of user's request from waste heat supply temperature.Because the complexity of heat pump causes utilizing heat pump to carry out UTILIZATION OF VESIDUAL HEAT IN and often invests higher.Adopting simple process flow as far as possible and structure is the most basic way that reduces equipment manufacturing cost, and this ability that also can make heat pump promote waste heat is improved simultaneously, and this can expand the scope of heat pump application.
Lower in residual heat resources relative deficiency, temperature, or the user's request temperature (initial temperature that comprises customer requirements, promptly enter the medium temperature of first kind absorption heat pump absorber) under the high situation, adopt the single-stage first kind absorption heat pump often can't be, also just can't reach and effectively utilize waste heat, realize energy-conservation purpose with the temperature increase of waste heat to the degree that the user needs.In the case, adopt the two-stage or the multi-stage first kind absorption heat pump of quick-reading flow sheets and structure can realize, thereby realize certain energy-saving benefit waste heat utilization to a certain degree.
Summary of the invention:
The objective of the invention is to provide simple two-stage of process structure and multi-stage first kind absorption heat pump, it can rise to the waste heat of lower temperature higher temperature, has expanded the scope of low temperature exhaust heat to high temperature user heat supply of utilizing.
The object of the present invention is achieved like this, and for enclosed two-stage and multi-stage first kind absorption heat pump, it mainly is made up of evaporimeter, absorption-evaporimeter, absorber, generator, condenser, choke valve, solution pump and solution heat exchanger (option); According to technological process, on entering flow process between evaporimeter and (one-level) absorption-evaporimeter from condensate liquid, be divided into two kinds of basic structures---a kind of is that condensate liquid is communicated with through the different choke valve of throttle degree respectively, and another kind is that choke valve adds the cryogen liquid pump and is communicated with.
Condensate liquid as shown in Figure 1 adopts in the enclosed two-stage first class absorption heat pump of two-way throttling, condenser has cryogen liquid pipeline to link to each other with absorption-evaporimeter with evaporimeter by choke valve respectively, evaporimeter also has the refrigerant vapour passage to link to each other with absorption-evaporimeter, there is the refrigerant vapour pipeline to link to each other respectively between absorption-evaporimeter and the absorber with the solution pipeline, be communicated with the solution pipeline by solution pump between absorption-evaporimeter and the generator, generator links to each other with absorber by the solution pipeline, generator has the refrigerant vapour passage to link to each other with condenser, there is the heated medium pipeline to link to each other between absorber and the condenser, it is characterized in that: the cryogen liquid that 1. comes from condenser, a part enters evaporimeter by the cryogen liquid pipeline that is communicated with between condenser and the evaporimeter through the throttling of the choke valve degree of depth, enters absorption-evaporimeter after the evaporation of absorption waste heat and is absorbed by the middle concentration solution from absorber, emit heat; Another part enters absorption-evaporimeter by the cryogen liquid pipeline that is communicated with condenser and absorption-evaporimeter through shallow degree throttling, becomes the higher refrigerant vapour of temperature after the heat absorption and enters absorber and absorbed, emit heat by the concentrated solution from generator; 2. the middle concentration solution that enters absorption-evaporimeter absorbs the low-pressure steam of flash-pot to become weak solution, squeeze into generator through solution pump, being discharged high-temperature steam after the external drive thermal source heating enters condenser, and the concentrated solution after concentration increases enters refrigerant vapour that absorber absorbs the higher temperature of self-absorption-evaporimeter, emits heat; 3. be heated fluid and at first enter the absorber heat absorption, and then enter the condenser heat absorption and make the high temperature refrigerant vapour that enters condenser be condensed into liquid.
Condensate liquid as shown in Figure 2 adopts in the enclosed two-stage first class absorption heat pump of throttle full open, a cryogen liquid pump pressure-raising, agent structure and technology and condensate liquid adopt the enclosed two-stage first class absorption heat pump basically identical of throttle style respectively, different is: structurally, be communicated with cryogen liquid pipeline by the cryogen liquid pump between evaporimeter and the absorption-evaporimeter; In technological process, the cryogen liquid that comes from condenser enters evaporimeter through the throttling of the choke valve degree of depth, wherein a part becomes cryogenic coolant steam after absorbing waste heat, enter absorption-evaporimeter then, the other part of vaporization does not enter absorption-evaporimeter through the suitable adherence pressure of cryogen liquid pump, vaporizing under higher temperature in the heat absorption back, enters absorber then.
Condensate liquid as shown in Figure 3 adopts in three grades of first kind absorption heat pumps of enclosed of three road throttle styles, condenser has cryogen liquid pipeline respectively by choke valve and evaporimeter, one-level absorption-evaporimeter links to each other with secondary absorption-evaporimeter, evaporimeter also has the refrigerant vapour passage to link to each other with one-level absorption-evaporimeter, there is the refrigerant vapour pipeline to link to each other respectively between one-level absorption-evaporimeter and the secondary absorption-evaporimeter with the solution pipeline, be communicated with the solution pipeline by solution pump between one-level absorption-evaporimeter and the generator, generator links to each other with absorber by the solution pipeline, generator has the refrigerant vapour passage to link to each other with condenser, absorber links to each other with secondary absorption-evaporimeter by the solution pipeline, there is the solution pipeline to link to each other respectively between secondary absorption-evaporimeter and the one-level absorption-evaporimeter with the refrigerant vapour pipeline, there is the heated medium pipeline to link to each other between absorber and the condenser, it is characterized in that: the cryogen liquid that 1. comes from condenser is divided into three parts, a part enters evaporimeter by the cryogen liquid pipeline that is communicated with between condenser and the evaporimeter through the throttling of the choke valve degree of depth, absorb and to enter one-level absorptions-evaporimeter after the waste heat evaporation by from the solution absorption of secondary absorption-evaporimeter and emit heat, another part enters one-level absorption-evaporimeter by the cryogen liquid pipeline that is communicated with condenser and absorption-evaporimeter through the shallow degree throttling of choke valve, becoming the higher refrigerant vapour of temperature after the heat absorption enters secondary absorption-evaporimeter and is absorbed by the solution from absorber and emit heat, again a part through choke valve more the throttling of low degree enter secondary absorption-evaporimeter, become the higher refrigerant vapour of temperature after the heat absorption, enter absorber then and absorbed from the concentrated solution of generator and emit heat; 2. the solution that enters one-level absorption-evaporimeter absorbs the low-pressure steam of flash-pot to become weak solution, squeeze into generator through solution pump, weak solution is discharged high-temperature steam after the heating of external drive thermal source and is entered condenser in generator, concentrated solution after concentration increases enters the refrigerant vapour of absorber absorption from the higher temperature of secondary absorption-evaporimeter, emit heat, solution after concentration reduces enters the refrigerant vapour of secondary absorption-evaporimeter absorption from one-level absorption-evaporimeter again, emit heat and make the cryogen liquid vaporization that enters secondary absorption-evaporimeter, solution after concentration reduces again enters the cryogenic coolant steam that one-level absorption-evaporimeter absorbs flash-pot, emit heat, and make the cryogen liquid vaporization that enters one-level absorption-evaporimeter; 3. be heated fluid and at first enter the absorber heat absorption, and then enter the condenser heat absorption and make the high temperature refrigerant vapour that enters condenser be condensed into liquid.
For open type two-stage and multi-stage first kind absorption heat pump, it is compared with multi-stage first kind absorption heat pump with corresponding enclosed two-stage, different is that the former has omitted evaporimeter than the latter, and one-level absorption-evaporimeter links to each other with the afterheat steam pipeline, and condenser coagulates water pipeline with waste heat and links to each other.
Description of drawings:
Fig. 1 is according to provided by the present invention, and condensate liquid adopts the enclosed two-stage first class absorption heat pump system architecture and the schematic flow sheet of two-way throttling, is an example.
Fig. 2 is according to provided by the present invention, and condensate liquid adopts the enclosed two-stage first class absorption heat pump system architecture and the schematic flow sheet of throttle full open, a cryogenic fluid pump liquid pressure-raising.
Fig. 3 is that condensate liquid adopts the enclosed three grades of first kind absorption type heat pump systems structure and the schematic flow sheet of three tunnel throttlings according to provided by the present invention.
Fig. 4 is according to provided by the present invention, and condensate liquid adopts the enclosed three grades of first kind absorption type heat pump systems structure and the schematic flow sheet of two-way throttling, a cryogen liquid pump pressure-raising.
Fig. 5 is that condensate liquid adopts the enclosed three grades of first kind absorption type heat pump systems structure and the schematic flow sheet of twice throttling, a cryogen liquid pump pressure-raising mode according to provided by the present invention.
Fig. 6 is that condensate liquid adopts the open type two-stage first class absorption heat pump system architecture and the schematic flow sheet of one tunnel throttling according to provided by the present invention.
Fig. 7 is according to provided by the present invention, and condensate liquid adopts the open type three grades of first kind absorption type heat pump systems structure and the schematic flow sheet of two-way throttling.
Fig. 8 is economic benefits and social benefits, enclosed two-stage first class absorption heat pump system architecture and the schematic flow sheet that adopts the two-way throttling according to condensate liquid provided by the present invention.
Fig. 9 is enclosed two-stage first class absorption heat pump system architecture and the schematic flow sheet that adopts the two-way throttling according to condensate liquid provided by the present invention, is another example.
Wherein, Fig. 3～Fig. 5 and Fig. 7 also are the representatives of multi-stage first kind absorption heat pump.
Among the figure, 1-evaporimeter, 2-(one-level) absorption-evaporimeters, 3-absorber, 4-generator, 5-condenser, 6-first throttle valve, 7-the second choke valve, 8-solution pump, 9-the first solution heat exchanger, 10-the second solution heat exchanger, 11-cryogen liquid pump, 12-secondary absorption-evaporimeter, 13-the three choke valve, 14-the three solution heat exchanger, 15-the four choke valve, 16-low pressure generator, 17-solution heat exchanger, 18-rectifying column, 20-cryogen liquid recirculation pump.
Wherein, solution heat exchanger and cryogen liquid recirculation pump belong to option, and the former is in order to improve unit performance, and the latter is in order to improve the effect that cryogen liquid absorbs waste heat.
The specific embodiment:
Describe the present invention in detail below in conjunction with accompanying drawing and example.
With provided by the present invention, it is example that condensate liquid adopts the enclosed two-stage first class absorption heat pump of two-way throttle style, as shown in Figure 1, the object of the present invention is achieved like this, 1. on the structure, this two-stage first class absorption heat pump is made up of evaporimeter 1, absorption-evaporimeter 2, absorber 3, generator 4, condenser 5, first throttle valve 6, second choke valve 7, solution pump 8 and first solution heat exchanger 9, second solution heat exchanger 10, auxiliary spare part and control corresponding systems such as the auxilliary pump in necessity, valve, pipe fitting; 2. the cryogen liquid from condenser 5 divides two-way respectively through entering evaporimeter 1 and absorption-evaporimeter 2 after the choke valve throttling---wherein one the tunnel through first throttle valve 6 carry out degree of depth throttling step-down, the cooling after enter evaporimeter 1, absorbing waste heat becomes cryogenic coolant steam, and then enter absorptions-evaporimeter 2 by from the solution absorption of absorber, emit heat; Another road cryogen liquid carries out entering absorption-evaporimeter 2 after the shallow degree throttling through second choke valve 7, and the steam that becomes higher temperature after the heat absorption enters absorber 3 and absorbed, emits heat by the solution from generator 4; 3. come the weak solution of self-absorption-evaporimeter 2, by solution pump 8 pressure-raisings, enter generator 4, externally drive and discharge the high temperature refrigerant vapour under the heat heating and enter condenser 5 through first solution heat exchanger 9; Concentrated solution enters absorber 3 through second solution heat exchanger 10, absorb the higher temperature of self-absorption-evaporimeter 2 steam, emit heat; The solution of intermediate concentration enters absorption-evaporimeter 2 through first solution heat exchanger 9, absorb flash-pot 1 Low Temperature Steam, emit heat; 4. be heated fluid and at first enter absorber 3 heat absorptions, and then enter condenser 5 externally outputs of heat absorption back, and make high temperature refrigerant vapour be condensed into liquid from generator 4.
As shown in Figure 2, condensate liquid adopts the enclosed two-stage first class absorption heat pump of a throttling, a cryogen liquid pump pressure-raising mode, there is not pipeline to link to each other between the condenser 5 that just is it with the former different and the absorption-evaporimeter 2, cryogen liquid all carries out degree of depth throttling by first throttle valve 6 before this and enters evaporimeter 1, wherein part absorption waste heat flashes to cryogenic coolant steam, and refrigerant vapour enters absorption-evaporimeter 2 and absorbed, emits heat by the solution from absorber 3; The cryogen liquid that another part is not vaporized enters absorption-evaporimeter 2 behind cryogen liquid pump 11 adherence pressures, heat absorption evaporation (higher temperature is correspondingly arranged) becomes the refrigerant vapour of higher temperature under suitable elevated pressures, and this part refrigerant vapour enters absorber 3 and absorbed by the solution from generator 4 and emit heat; The two is as broad as long on other flow process.
As shown in Figure 3, in three grades of first kind absorption heat pumps of enclosed, 1. on the structure, these three grades of first kind absorption heat pumps are made up of evaporimeter 1, one-level absorption-evaporimeter 2, absorber 3, generator 4, condenser 5, first throttle valve 6, second choke valve 7, solution pump 8, first solution heat exchanger 9, second solution heat exchanger 10, secondary absorption-evaporimeter 12, the 3rd choke valve 13 and the 3rd solution heat exchanger 14, auxiliary spare part and control corresponding systems such as the auxilliary pump in necessity, valve, pipe fitting; 2. the cryogen liquid from condenser 5 divides three the tunnel respectively through entering evaporimeter 1, one-level absorption-evaporimeter 2 and secondary absorption-evaporimeter 3 after the choke valve throttling---wherein one the tunnel through first throttle valve 6 carry out degree of depth throttling step-down, the cooling after enter evaporimeter 1, absorbing waste heat becomes cryogenic coolant steam, and then enter one-level absorptions-evaporimeter 2 by from the solution absorption of secondary absorption-evaporimeter 12, emit heat; Another road cryogen liquid carries out entering one-level absorption-evaporimeter 2 after the shallow degree throttling through second choke valve 7, and the steam that becomes higher temperature after the heat absorption enters secondary absorption-evaporimeter 12 and absorbed, emits heat by the solution from absorber 3; One the tunnel after saving the throttling that the 3rd stream valve 13 carries out low degree more, enter secondary absorptions-evaporimeter 12 again, become the higher refrigerant vapour of temperature after the heat absorption, enter absorber 3 then by from the concentrated solution absorption of generator 3 and emit heat; 3. from the weak solution of one-level absorption-evaporimeter 2, by solution pump 8 pressure-raisings, enter generator 4, externally drive and discharge the high temperature refrigerant vapour under the heat heating and enter condenser 5 through first solution heat exchanger 9; Concentrated solution enters absorber 3 through second solution heat exchanger 10, absorbs steam from the higher temperature of secondary absorption-evaporimeter 12, emits heat; Solution after concentration is thinning enters secondary absorption-evaporimeter 12 through the 3rd solution heat exchanger 14, absorbs Low Temperature Steam from one-level absorption-evaporimeter 2, emits heat; Solution after concentration is further thinning enters one-level absorptions-evaporimeter 2 through first solution heat exchanger 9, absorption come flash-pot 1 cryogenic coolant steam, emit heat; 4. be heated fluid and at first enter absorber 3 heat absorptions, and then enter condenser 5 externally outputs of heat absorption back, and make high temperature refrigerant vapour be condensed into liquid from generator 4.
On structure, in two-stage and multi-stage first kind absorption heat pump among the present invention, along with the increase of progression, the quantity of absorption-evaporimeter also increases, for progression subtracts 1.
From flow process, the concrete workflow of each fluid is as follows:
1. waste heat medium flow process---waste heat medium enter evaporimeter 1 heating through first throttle valve 6 carry out degree of depth throttling refrigerant medium, make it be vaporized into cryogenic coolant steam; The cryogenic coolant medium enters (one-level) absorption-evaporimeter and is absorbed the heat emit higher temperature by solution and make another road refrigerant medium that enters absorptions-evaporimeter higher steam of formation temperature that obtains vaporizing, and has realized the first order lifting of waste heat supply temperature; Along with the increase of absorption-evaporimeter, waste heat is promoted step by step.
2. the high-temperature medium flow process---high temperature driven heat enters generator 4, finishes the heating to the weak solution of coming self-absorption-evaporimeter 2, and the refrigerant vapour that produces high temperature enters condenser 5.
3. the heated medium flow process---heated medium at first enters absorber 3, draw liberated heat in the refrigerant vapour process that concentrated solution absorbs self-absorption-evaporimeter 2, then enter condenser 5, draw from externally output after the heat release of the high temperature refrigerant vapour of generator.
4. the refrigerant vapour flow process---the high temperature refrigerant vapour from generator 4 adds hot fluid in condenser 5, condensation becomes liquid, divides two-way to enter evaporimeter 1 and absorption-evaporimeter 2 respectively after the throttling that first throttle valve 6 and second choke valve 7 carry out in various degree; The refrigerant medium that enters evaporimeter 1 is heated and is vaporized into cryogenic coolant steam, enters absorption-evaporimeter 2, is absorbed by the solution from the higher concentration of absorber 3, emits heat; Enter the refrigerant medium of absorption-evaporimeter 2, draw the refrigerant vapour that becomes higher temperature in the absorption process behind the liberated heat, enter absorber 3 and absorbed, emit the heated medium that the heat heating enters by concentrated solution from generator 4.
5. the solution flow process---the concentrated solution that comes from generator 4 enters absorber 3 through second solution heat exchanger 10, concentration reduces after absorbing the refrigerant vapour of higher temperature of self-absorption-evaporimeter 2, enter absorption-evaporimeter 2 through first solution heat exchanger 9, absorbing becomes weak solution behind the cryogenic coolant steam of flash-pot 1, by solution pump 8, behind first solution heat exchanger 9, second solution heat exchanger 10, squeeze into generator 4, under the heating that drives heat, discharge the high temperature refrigerant vapour, then become the solution of high concentration again.
Figure 4 shows that condensate liquid adopts three grades of first kind absorption type heat pump systems of enclosed of two-way throttling, a cryogen liquid pump pressure-raising, the difference of it and flow process shown in Figure 3 is: the cryogen liquid from condenser 5 divides the two-way throttling to enter evaporimeter 1 and secondary absorption-evaporimeter 12 respectively; Wherein enter the refrigerant medium of evaporimeter 1, a part is the heat absorption vaporization in evaporimeter 1, another part enters one-level absorption-evaporimeter 2 again after cryogen liquid pump 11 carries out suitable pressure-raising, heat absorption is vaporized into the higher refrigerant vapour of temperature to be provided to secondary absorption-evaporimeter 12.
Figure 5 shows that condensate liquid adopts three grades of first kind absorption heat pumps of enclosed of twice throttling, a cryogen liquid pump pressure-raising mode, the difference of it and flow process shown in Figure 4 is: enter evaporimeter 1 after the whole throttlings of cryogen liquid from condenser 5, wherein enter the refrigerant medium of evaporimeter 1, part heat absorption vaporization in evaporimeter 1, another part divide two-way respectively through 15 throttlings of the 4th choke valve with directly enter one-level absorption-evaporimeter 2 and secondary absorption-evaporimeter 12 again after cryogen liquid pump 11 carries out suitable pressure-raising; Enter one road refrigerant medium of one-level absorption-evaporimeter 2, be vaporized into the higher refrigerant vapour of temperature after the heat absorption and enter secondary absorption-evaporimeter 12, directly enter the cryogen liquid on another road of secondary absorption-evaporimeter 12, pressure is higher, and heat absorption is vaporized into the higher refrigerant vapour of temperature to be provided to absorber 3.
Figure 6 shows that condensate liquid adopts the open type two-stage first class absorption heat pump of one tunnel throttling, it and different being shown in Figure 1: do not had evaporimeter 1 on the structure, afterheat steam directly absorbs-evaporimeter 2, finishes self cooling condenser 5 outputs after the effect of waste heat medium; Cryogen liquid directly enters absorption-evaporimeter 2 after 7 throttlings of second choke valve, heat absorption becomes refrigerant vapour to be provided to absorber 3.
Figure 7 shows that condensate liquid adopts three grades of first kind absorption heat pumps of open type of two-way throttling, the difference of it and flow process shown in Figure 3 is: do not had evaporimeter 1 on the structure, afterheat steam directly carries out one-level absorption-evaporimeter 2, finishes self cooling condenser 5 outputs after the effect of waste heat medium; Cryogen liquid from condenser 5 divides the two-way throttling to enter one-level absorption-evaporimeter 2 and secondary absorption-evaporimeter 12 respectively.Wherein enter the refrigerant medium of absorption-evaporimeter 2, heat absorption becomes refrigerant vapour to be provided to secondary absorption-evaporimeter 12; Entering cryogen liquid heat absorption in the secondary absorption-evaporimeter 12 after 13 throttlings of the 3rd choke valve is vaporized into the higher refrigerant vapour of temperature and provides to absorber 3.
Figure 8 shows that condensate liquid adopts economic benefits and social benefits, the enclosed two-stage first class absorption heat pump of two-way throttling, it and different being shown in Figure 1, the high temperature refrigerant vapour that produces in the generator 4 does not directly enter condenser 5, realizes the economic benefits and social benefits effect but enter low pressure generator 16.Heat pump more shown in Figure 1, this economic benefits and social benefits two-stage (and multistage) heat pump complex structure, heat supply temperature is low, and manufacture difficulty strengthens, and cost is also high.
Figure 9 shows that the two-stage first class absorption heat pump of mainly forming by evaporimeter, absorption-evaporimeter, absorber, rectifying column, condenser, choke valve, solution pump and solution heat exchanger, it and difference shown in Figure 1 are that it can adopt with the ammonia spirit is representative, the working medium that need carry out rectification process.
The effect that the technology of the present invention can realize---two-stage and multi-stage first kind absorption heat pump proposed by the invention have following effect and advantage:
1. simple in structure, flow process is reasonable, can reduce equipment manufacturing cost.
2. can realize two-stage and the Multi-stage lifting of waste heat supply temperature.
3. can reduce the temperature of concentrated solution in the generator, avoid or reduce the corrosion that solution herein may cause equipment, carry High device security.
4. can utilize the waste heat of lower temperature and the heat supply that provides higher temperature to the user, enlarge first kind absorption type heat The temperature working range of pump.
Claims (1)
1. two-stage and multi-stage first kind absorption heat pump mainly are made up of in conjunction with cryogen liquid pump, solution pump and solution heat exchanger evaporimeter, absorption-evaporimeter, absorber, generator, condenser, choke valve or choke valve; In two-stage first class absorption heat pump, condenser (5) or have cryogen liquid pipeline to link to each other with absorption-evaporimeter (2) with evaporimeter (1) with second choke valve (7) through first throttle valve (6) respectively, or there is cryogen liquid pipeline to link to each other with evaporimeter (1) and evaporimeter (1) has cryogen liquid pipeline to be communicated with absorption-evaporimeter (2) through cryogen liquid pump (11) again through first throttle valve (6), evaporimeter (1) has the refrigerant vapour passage to link to each other with absorption-evaporimeter (2) and has surplus heat medium pipeline and external communications, pass through solution pump (8) between absorption-evaporimeter (2) and the generator (4), first solution heat exchanger (9) and second solution heat exchanger (10) are communicated with the solution pipeline, through second solution heat exchanger (10) the solution pipeline connection is arranged between generator (4) and the absorber (3), there is solution pipeline to link to each other through first solution heat exchanger (9) between absorber (3) and the absorption-evaporimeter (2), also have the refrigerant vapour passage to link to each other between absorber (3) and the absorption-evaporimeter (2), generator (4) also has the refrigerant vapour passage to link to each other with condenser (5) and the hot medium pipeline of driving and external communications is arranged, and absorber (3) and condenser (5) also have heated medium pipeline and external communications respectively; In three grades of first kind absorption heat pumps, condenser (5) has cryogen liquid pipeline to be communicated with evaporimeter (1) through first throttle valve (6), or directly link to each other with secondary absorption-evaporimeter (12) with one-level absorption-evaporimeter (2) with the 3rd choke valve (13) through second choke valve (7) respectively by condenser (5), or by evaporimeter (1) through cryogen liquid pump (11) with directly link to each other with secondary absorption-evaporimeter (12) with one-level absorption-evaporimeter (2) respectively through the 3rd choke valve (13) by condenser (5), or directly be communicated with secondary absorption-evaporimeter (12) and in conjunction with the 4th choke valve (15) indirect communication one-level absorption-evaporimeter (2) through cryogen liquid pump (11) by evaporimeter (1), evaporimeter (1) also has refrigerant vapour channel connection one-level absorption-evaporimeter (2) and have surplus heat medium pipeline and external communications, one-level absorption-evaporimeter (2) is through solution pump (8), first solution heat exchanger (9), the 3rd solution heat exchanger (14) and second solution heat exchanger (10) are communicated with generator (4), through second solution heat exchanger (10) the solution pipeline connection is arranged between generator (4) and the absorber (3), there is solution pipeline to link to each other and absorber (3) and secondary absorption-evaporimeter (12) also have the refrigerant vapour channel connection between the two through the 3rd solution heat exchanger (14) between absorber (3) and the secondary absorption-evaporimeter (12), there is solution pipeline to link to each other and secondary absorption-evaporimeter (12) and one-level absorption-evaporimeter (2) also have the refrigerant vapour channel connection between the two through first solution heat exchanger (9) between secondary absorption-evaporimeter (12) and the one-level absorption-evaporimeter (2), generator (4) also has the refrigerant vapour passage to link to each other with condenser (5) and the hot medium pipeline of driving and external communications is arranged, and absorber (3) and condenser (5) also have heated medium pipeline and external communications respectively; It is characterized in that: during two-layer configuration, cryogen liquid provides refrigerant vapour to absorption-evaporimeter (2) and absorber (3) respectively after the heat absorption vaporization respectively in evaporimeter (1) and absorption-evaporimeter (2), weak solution is through solution pump (8), first solution heat exchanger (9) and second solution heat exchanger (10) enter generator (4), the high temperature refrigerant vapour that discharges that is heated enters condenser (5), and concentrated solution enters absorber (3) and enters absorption-evaporimeter (2) through first solution heat exchanger (9) through second solution heat exchanger (10) successively, finish absorption respectively to the refrigerant vapour that enters; During tertiary structure, cryogen liquid is respectively in evaporimeter (1), in one-level absorption-evaporimeter (2) and the secondary absorption-evaporimeter (12) after the heat absorption vaporization respectively to one-level absorption-evaporimeter (2), secondary absorption-evaporimeter (12) and absorber (3) provide refrigerant vapour, weak solution is through solution pump (8), first solution heat exchanger (9), the 3rd solution heat exchanger (14) and second solution heat exchanger (10) enter generator (4), the weak solution high temperature refrigerant vapour that discharges that is heated enters condenser (5), and concentrated solution enters absorber (3) through second solution heat exchanger (10) successively, enter secondary absorption-evaporimeter (12) and enter one-level absorption-evaporimeter (2) through the 3rd solution heat exchanger (14) and finish absorption respectively the refrigerant vapour that enters through first solution heat exchanger (9).
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|---|---|---|---|---|
| CN101545693B (en) * | 2007-08-27 | 2010-12-08 | 李华玉 | Heterogeneous composite absorption type heat pump |
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| CN101520251B (en) * | 2009-03-18 | 2011-01-26 | 李华玉 | Generation-absorption-reabsorption system and absorption unit type based on system |
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| CN101825369A (en) * | 2010-04-02 | 2010-09-08 | 清华大学 | High-efficiency compact high-temperature absorption type heat pump unit |
| CN101957093B (en) * | 2010-08-13 | 2013-05-29 | 李华玉 | Absorption-reabsorption-generation system and first-class absorption heat pump |
| CN102230686A (en) * | 2011-06-12 | 2011-11-02 | 浙江理工大学 | Lithium bromide absorption-compression type series boosting refrigeration/heating pump system |
| WO2014089721A1 (en) * | 2012-12-10 | 2014-06-19 | Li Huayu | Multi-effect first-type absorption heat pump |
| CN103148630B (en) * | 2013-02-26 | 2015-08-12 | 李华玉 | Composite-generationsecond second kind absorption type heat pump |
| CN103196256B (en) * | 2013-03-09 | 2015-08-12 | 李华玉 | Composite-generationsecond second kind absorption type heat pump |
| CN104180561B (en) * | 2014-09-05 | 2016-04-13 | 哈尔滨工业大学 | A kind of cold double-effect lithium bromide absorption type cooling cycle system |
| CN104180555B (en) * | 2014-09-05 | 2016-04-13 | 哈尔滨工业大学 | A kind of cold dual effect type lithium bromide jet suction type cooling cycle system |
| WO2018150516A1 (en) * | 2017-02-16 | 2018-08-23 | 日立ジョンソンコントロールズ空調株式会社 | Absorption refrigerator |
| CN113324346B (en) * | 2021-05-20 | 2022-06-14 | 浙江理工大学 | Double-effect/two-stage open type absorption heat pump |
| CN113280395B (en) * | 2021-05-21 | 2022-10-25 | 西安交通大学 | Hot water boiler system of coupling absorption type lithium bromide heat pump device |
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2006
- 2006-11-24 CN CNB2006100704289A patent/CN100504242C/en active Active
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