CN1414326A - Multistage absorption type refrigerating apparatus - Google Patents
Multistage absorption type refrigerating apparatus Download PDFInfo
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- CN1414326A CN1414326A CN01133610A CN01133610A CN1414326A CN 1414326 A CN1414326 A CN 1414326A CN 01133610 A CN01133610 A CN 01133610A CN 01133610 A CN01133610 A CN 01133610A CN 1414326 A CN1414326 A CN 1414326A
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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 invented multistage adsorption type refrigerating device uses lithium bromide or diethaneolamine or triethanolamine as working medium, the said device includes three generators, two or three evaporators, two or three absorbers, one condensor, four heat exchangers and their connected mechanical pump, valve, instrument, pipeline; it adopts triple-effect generation, two-stage or three-stage evaporation, two-stage or three-stage absorption flowpath, that is two-stage absorption or three stage absorption type, the three-stage absorption divides the user as high temperature air conditioning refrigerating region and low temperature air conditioning region or divides as high temperature, medium temperature, low temperature air conditioning refrigerating region. It can save energy by 40-50%.
Description
Technical field
The present invention relates to use the apparatus of binary solution as the absorption refrigeration of working medium.
Background technology
Utilize the absorption refrigeration of binary solution such as lithium bromide water solution for working medium, it is the method for generally using in the large-size air conditioning system in recent years, except these working medium have the benefit that can replace at present the fluorocarbons of atmospheric ozone damage layer, their characteristics also are to make full use of the thermal source of lower temperature, for example utilize the low-pressure steam of factory, boiler flue, also can utilize combustion gas, fuel oil is as thermal source, in possible place, also can utilize the thermal source of solar energy as refrigeration, absorption refrigeration operates steadily in addition, cost is lower, operate also simply relatively, be used for large-scale hotel at present, the market, the air-conditioning system in commercial building etc.Present being seen absorption system mainly uses one section evaporation, one section method that absorption, two effects take place, promptly in generator, utilize thermal source that binary working medium solution is heated, produce water vapour, in condenser, use cooling water to cool off indirectly then, water vapour is condensed into liquid, behind choke valve, expand again, in evaporimeter, absorb the heat refrigeration, and become steam, and entering absorber, the concentrated solution absorption of being sent here in the generator also becomes weak solution, weak solution with pump draw back generator carry dense, like this circularly cooling.Because this one section evaporation, one section absorption refrigeration method exist the absorber concentration difference and temperature difference is little, the regenerator heat dissipation is bigger, thereby causes refrigerating efficiency not high, and the thermal source utilization is also abundant inadequately.
Imitate the weak point that refrigerating methods take place at above-mentioned one section evaporation, one section absorption, two, people have also carried out some improvement to it at present, with one section evaporation, absorb and change two sections or three sections evaporations, absorption into.A kind of multi-stage absorption refrigeration machine is disclosed as Chinese patent 95215192.8.It is the space of being made up of evaporimeter, absorber adjacent, two spaces are communicated with throttle pipe, and play the water seal effect, and are too high for preventing strong solution concentration, system also is provided with diluter, the advantage of this absorption type refrigerating unit is to increase than the single-stage absorption refrigerating machine thermal efficiency, and heat exchanger area is less, and the solution circulation is easier to, but it is complicated that its shortcoming is the absorber structure, in fact do not reach dual circulation, the effect of two sections absorptions, the thermal efficiency improves not obvious.
Chinese patent 97199362.9 discloses a kind of triple effect absorbent refrigeration system, its process is that solution flows to first and second generators that are connected in parallel from an absorber, the solution that comes out from first generator turns back to the absorber, the solution that comes out from second generator flows to the 3rd generator that is connected in series with this second generator, refrigerant vapour condensation in corresponding condenser from each generator, the 3rd condenser and the second generator heat-shift, and second condenser and the first generator heat-shift, the benefit of this triple effect absorbent refrigeration system is relatively to have made full use of effective heat, the generator thermal efficiency is improved, but shortcoming is that energy-conservation is unconspicuous owing to deliver to the not minimizing of weak solution internal circulating load of generator.
Chinese patent 98111110.6 is a kind of two sections or multi-section hot water lithium bromide absorbing refrigerating units, it has comprised pipeline, pump, the valve of two or more generators, condenser, evaporimeter, absorber, solution heat exchanger and connection, hot-water heating system is connected a plurality of generators, chilled water system links to each other a plurality of evaporimeters, and the cooling water parallel connection is connected with two or more condensers, absorber respectively.Hot water, cold water, cooling water are lowered the temperature in one or more self-contained refrigerating systems, are heated up, thereby the hot water temperature is even lower, heat utilization is better, but the refrigerating plant of this structure is little owing to the absorbent solution concentration difference changes, thereby does not also reach energy-saving effect preferably.
Two sections of above-mentioned open source literature report or three sections absorbent refrigeration systems and device exist that to absorb the operation temperature range little, the absorbent solution concentration difference is also less, energy-conservation inadequately significantly and use shortcomings such as cooling water inflow is more, thereby the refrigeration system that up to the present absorbs more than two sections or two sections fails to be applied.
Technology contents
In order to overcome the weak point of prior art, the inventor is through testing and study refrigerating method and refrigeration working medium for many years, designed the refrigeration process flow process that a kind of triple effect takes place, two sections (or three sections) evaporate, two sections (or three sections) absorb, this technological process can use lithium bromide to be working medium, also can use diethanol amine, triethanolamine or the material with similarity are cold-producing medium working medium, can save cooling water amount greatly after using this cover technology, and have obvious energy-saving effect.
Technical scheme of the present invention is achieved in that
Multistage absorption type refrigerating apparatus, it comprises: three generators, two or three evaporimeters, two or three absorbers, a condenser, four heat exchangers, and the pump that connects with it, valve, instrument, pipeline: adopt two sections or three sections absorption, promptly adopt triple effect to take place, two sections or three sections evaporations, the mode of two sections or three sections absorptions, two or three evaporimeters and two or three absorbers are installed in the container, separate with dividing plate the centre, the triple effect generator is divided into high pressure generator, middle generator and the low pressure generator of pressing, high pressure generator independently separately, middle generator and the low pressure generator of pressing can separate separately, also can be integrated, be installed in the container, the centre separates with dividing plate, condenser then is contained in the container jointly with low pressure generator, high pressure, the middle pressure, the connection of three generators of low pressure, adopt forward and crossfire journey, be that high pressure generator is in parallel with low pressure generator, the middle generator of pressing is connected with high pressure generator, or employing is reverse and the crossfire journey, press generator in parallel promptly with low pressure generator, high pressure generator is connected with middle pressure generator, or adopts three generators flow process all in parallel.Two or three evaporimeters are coupled in series, and two or three absorbers also are coupled in series.Cooling water enters from one section absorber, leads to two sections absorbers again, after (or leading to three sections absorbers again), is sent to condenser again, and it is recycling that the cooling water after the intensification leads to cooling tower cooling back.The cold water that comes from colod-application family, from high section to low section successively through each section evaporimeter, promptly successively through flash evaporator, one section evaporimeter, or successively through three sections evaporimeters, flash evaporator, one section evaporimeter, cold water is through two (two sections, one section) evaporimeters, or through three (three sections, two sections, one section) evaporimeters, temperature is sent colod-application family (as hotel, commercial building, large-scale public place of entertainment etc.) after reaching required low temperature, as cold source of air conditioning, cold water is also recycling; Each section evaporimeter and each section absorber are all established a circulation infusion pump; The taphole of triple effect (three) generator is equipped with heat exchanger, and the refrigerant vapour condensation mixed liquor of the 4th heat exchanger with pressure, low pressure generator in utilizing is set, and heating enters the rare working medium solution before the low pressure generator.Two sections (or three sections) absorbers and condenser are provided with air extractor.When adopting three sections absorption schemes, colod-application family need be divided into the high-temperature air conditioner refrigeration area, low-temperature air conditioner refrigeration area, (or being divided into high temperature, middle temperature, low-temperature air conditioner refrigeration area).
The thermal source of high pressure generator can adopt direct heat source, as direct-fired combustion gas, fuel oil, also can adopt indirect thermal source, as steam, hot water etc., also can use solar water.(with diethanol amine, triethanolamine is that working medium can only adopt thermal source indirectly such as steam, hot water).
Employed refrigeration working medium also can use diethanol amine, triethanolamine except that lithium bromide.
The operation principle of absorption refrigerator of the present invention is: (with two sections absorption be example)
Send dense refrigeration working medium solution here from generator and be sent to one section absorber, the refrigerant vapour that absorption comes from one section evaporimeter, the solution quilt first time is towards rare, this solution enters two sections absorbers then, absorb the refrigerant vapour that comes from flash evaporator once more, solution is once more by towards rare, the weak solution of coming out from two sections absorbers is pumped to triple effect (three) generator with generator pump and high pressure generator and carries dense, wherein high pressure generator is in parallel with low pressure generator, the middle generator of pressing is connected with high pressure generator, be that the solution that high pressure generator comes out enters the middle generator of pressing, the concentrated solution of therefrom pressing generator and low pressure generator to come out enters one section absorber simultaneously, begins new circulation.
The cold water that comes from the colod-application family of needs refrigeration enters flash evaporator and one section evaporimeter lower the temperature at twice after, reach required low temperature, send colod-application family again back to.
The cooling water that comes from cooling tower is successively through one section absorber, two sections absorbers, condenser, delivers to cooling tower again after heating up for three times.
Compared with prior art, outstanding substantive distinguishing features of the present invention and obvious improvement are:
1, open source literature and the actual lithium bromide absorbing type refrigeration technology of using mainly are the cooling flows that economic benefits and social benefits take place, single hop evaporates, single hop absorbs at present, the venting scope is at 4-5.5%, and its energy consumption is higher, and cooling water amount is big, the present invention on the basis of existing technology, carry out multinomial improvement, (1) is imitated by two and is changed the triple effect generation into, and (2) are evaporated by single hop, single hop absorbs and changes two section evaporations into, two sections absorptions, (3) suitably improve cryogenic temperature on the basis that does not influence refrigeration.Improve the back and compare with the flow process that the above-mentioned economic benefits and social benefits of mentioning take place, single hop evaporates, single hop absorbs, the venting scope is brought up to more than 7% or 7% by 4-5.5%, and consumption of cooling-water saves about 50%, and total energy consumption saves about 40%.
2, compare with disclosed patent documentation, as No. 95215192.8 patents, " multi-stage absorption refrigeration machine " (two sections are steamed receipts, two sections absorptions) and two sections or multi-section hot water lithium bromide absorbing refrigerating unit (multi-stage evaporation of No. 98111110.6 patents, multistage absorbs) compare, in fact these two patents do not reach two sections or multi-stage evaporation, the effect that absorbs, the problem of most critical be the solution concentration difference obviously do not improve (because of evaporimeter pump and absorber shared), the venting scope does not just improve, the solution internal circulating load does not reduce, so thermodynamic coefficient and energy-conservation raising are all not obvious; And No. 97199362.9 patents are also because only design triple effect generation separately, do not design two-stage evaporation, two sections absorptions, energy-conservation also very limited, this patent has two shortcomings in addition: one, the high pressure generator pump is at high temperature operated (about 150-160 ℃), the material of pump requires high, it is dangerous to turn round, damage easily, two, the utilization of refrigerant vapour condensate heat is abundant inadequately, and the present invention can overcome the shortcoming of above-mentioned patent, be that the high pressure generator pump is operated at normal temperatures, the heat of refrigerant vapour condensate liquid is fully used, thereby reduces the thermic load of low pressure generator.
3, two of this Refrigeration Technique sections absorption, promptly adopt triple effect generation, two-stage evaporation, two sections absorptions theoretically be feasible in the practice, a high pressure generator takes place to need to increase though change triple effect into from two effects, the operating pressure of high pressure generator is about 0.9Mpa, (gauge pressure) operating temperature is about 200 ℃, yet these conditions can realize fully; In addition, triple effect takes place improving thermodynamic coefficient and energy-conservation all more favourable, and it takes place energy-conservation more remarkable compared with two effects of prior art.
Again from two-stage evaporation, see in the operating practice of two sections absorptions, one section evaporation, the operating pressure of one section absorption, operating temperature control relatively is lower, to obtain required cryogenic refrigeration temperature, and dual circulation, two sections absorptions just can be controlled higher operating pressure and operating temperature, this just means after two sections absorptions, the solution concentration difference improves greatly, the venting scope has also been improved, and the weak solution internal circulating load of promptly delivering to generator significantly reduces, and the refrigeration that with working medium is lithium bromide is an example, when using the single hop evaporation, when single hop absorbed operation, the 1kg refrigerant vapour took place in generator, need deliver to the about 15kg of weak solution of generator, but use two section evaporations, two sections absorptions, when triple effect takes place, the 1kg refrigerant vapour takes place in same refrigeration, and the weak solution that need deliver to generator then is reduced to about 9kg by about 15kg, it is about 35～40% that the weak solution amount reduces, thereby the thermic load of generator just greatly reduces.Simultaneously because the raising of two sections absorption temperature, cooling range is improved, originally cooling water is through the absorber temperature difference about 4 ℃, after adopting two sections absorptions, cooling range through absorber can be brought up to 7-8 ℃, so cooling-water consumption just can save about 50%, adds other conservation measures, Refrigeration Technique of the present invention can save energy about 40%, and thermodynamic coefficient reaches more than 1.7 or 1.7.
4, to some colod-application family, can be divided into high-temperature air conditioner refrigeration area, low-temperature air conditioner refrigeration area (or being divided into high temperature, middle temperature, low-temperature air conditioner refrigeration area) to colod-application family, this moment can adopt three sections absorption, promptly adopt triple effect generation, three sections evaporations, three sections absorption flow processs, three sections evaporimeters and three sections absorbers all adopt coupled in series.Schematic flow sheet is an example with lithium bromide working medium still as shown in Figure 5, adopt three sections absorption, its cooling water saving is more, the venting scope more can improve.With economic benefits and social benefits generation, single hop evaporation, single hop absorption refrigeration technology is compared, and advances generator weak solution internal circulating load and reduces 50% approximately, and comprehensive energy consumption saves about 50%.
Description of drawings
Fig. 1 is a kind of enforcement structure chart of refrigerating plant of the present invention, and high pressure generator separates separately, middle pressure generator, and low pressure generator and condenser are installed in the scheme of same container, and generator adopts forward and crossfire journey.
Fig. 2 is that second kind of refrigerating plant of the present invention implemented structure chart, and high pressure generator, middle pressure generator all independently separate, and low pressure generator and condenser are installed in the scheme in the same container, and generator also adopts forward and crossfire journey.
Fig. 3 is the third enforcement structure chart of refrigerating plant of the present invention, and generator adopts oppositely and the crossfire journey.
Fig. 4 is that the 4th kind of refrigerating plant of the present invention implemented structure chart, and generator adopts typical shunting (parallel connection) flow process.
Fig. 5 is three sections absorption flow schemes, colod-application family is divided into high-temperature air conditioner refrigeration area, low-temperature air conditioner refrigeration area, or be divided into high temperature, middle temperature, low-temperature air conditioner refrigeration area, and three evaporimeters and three absorbers are installed in the container, and generator connection and all the other structures are with Fig. 1 or Fig. 2.
The specific embodiment
Further specify the course of work of refrigerating plant of the present invention with five Figure of description:
Fig. 1 (embodiment example one), as shown in the figure,
Schematic flow sheet is as shown in Figure 1: the vapour agent steam (sweat cooling) that one section evaporimeter (1) evaporates enters one section absorber (4) and is absorbed by the dense lithium-bromide solution of spray in this absorber, the lithium-bromide solution quilt first time is towards rare, this weak solution is delivered to two sections absorbers (5), spray absorbs the refrigerant vapour (sweat cooling too) that comes from flash evaporator (2) once more, and solution is once more by towards rare.The rare lithium-bromide solution that comes out from two sections absorbers divides two-way to send with generator pump (21).The first via is pressurizeed once more with the high pressure generator pump (22) of relay, successively through second heat exchanger (12), entering high pressure generator (7) behind first heat exchanger (11) twice heat temperature raising carries dense for the first time, the intermediate solution of coming out from high pressure generator presses generator (8) to carry dense once more after first heat exchanger heat exchange cooling in entering.The second the tunnel through the 3rd heat exchanger (13), enter low pressure generator (9) behind the 4th heat exchanger (14) twice heat temperature raising and carry dense.Therefrom press generator, low pressure generator to come out dense lithium-bromide solution respectively after second heat exchanger (12), the 3rd heat exchanger (13) heat exchange cooling, be pooled to one section absorber, constituted the cyclic process of lithium-bromide solution.
One section evaporimeter (1) and flash evaporator (2) refrigerant vapour that sweat cooling was evaporated are absorbed by the lithium-bromide solution of one section absorber (4), two sections absorbers (5) respectively uses generator pump (21), high pressure generator pump (22) to be delivered to three generators towards rare lithium-bromide solution and carry dense having absorbed refrigerant vapour then.From the refrigerant vapour that high pressure generator (7) comes out, press generator (8) in causing, and press the heating thermal source of generator in the conduct.The refrigerant vapour of therefrom pressing generator (8) to come out causes low pressure generator (9), as the heating thermal source of low pressure generator.The refrigerant vapour that low pressure generator (9) comes out causes condenser (10), is condensed into water as refrigerant with the indirect cooling of cooling water.Also be condensed into water as refrigerant after utilizing its latent heat as the thermal source refrigerant vapour of middle pressure, low pressure generator, be mixed together through the 4th heat exchanger (14), after utilizing its heat, also enter condenser (10), deliver to one section evaporimeter (1) and flash evaporator (2) from the water as refrigerant that condenser comes out, constituted the cyclic process of water as refrigerant again.
The thermal source of high pressure generator can be indirect thermal source (steam, a hot water etc.), also can be direct-fired direct heat source (combustion gas, fuel oil etc.).(adopting diethanol amine, triethanolamine is working medium, can only use indirect thermal source)
The cold water that comes from colod-application family is sent colod-application family through flash evaporator (2) again back to after one section evaporimeter (1) twice cooling reaches required low temperature.
Send cooling tower back to from the cooling water (about 32 ℃) (temperature reaches about 42 ℃) after one section absorber (4), two sections absorbers (5), condenser heat up for (10) three times that cooling tower comes.Air extractor (23) is an oil-sealed rotary pump, and it is bled to satisfy one section absorber (4), two sections absorbers (5), the needed low pressure of condenser (10) (vacuum).
Fig. 1 to Fig. 4 is two sections absorption schemes, one, flash evaporator and one, two section absorber all place in the same container, and this is an identical point, its difference then is presented in each accompanying drawing.
Fig. 1 generator adopts forward and crossfire journey, and promptly the pressure generator is connected with high pressure generator in high pressure generator and the low pressure generator parallel connection.This figure is the preferred embodiment of the invention, and its heat utilization is better, operates more convenient.
Fig. 2 is on the basis of Fig. 1, in press generator to tell independent setting, have outside the advantage identical with Fig. 1, the advantage of pressing generator to be convenient to be incubated in also having, its shortcoming is that equipment expands, cost is higher.
Fig. 3, generator adopt oppositely and the crossfire journey, and promptly middle pressure generator is in parallel with low pressure generator, and high pressure generator is connected with middle pressure generator.It has heat utilization same as in figure 1 advantage preferably, and its shortcoming is the pump operated temperature of high pressure generator higher (150～160 ℃), and material is required height, and is easy to damage.
Fig. 4, generator adopt shunting flow process in parallel, and ie in solution divides three the tunnel, high pressure, middle pressure, the low pressure generator of coming in and going out in parallel.Its advantage is that flow process is simple, easy to operate, and its shortcoming is the cold and heat solution heat exchange of first heat exchanger, and the temperature difference is big, and heat loss is big.
Fig. 5 adopts three sections absorption schemes, and colod-application family is divided into high-temperature air conditioner refrigeration area, low-temperature air conditioner refrigeration area, or is divided into high temperature, middle temperature, low-temperature air conditioner refrigeration area.Triple effect generation, three sections evaporations, three sections absorptions are set, and three evaporimeters are coupled in series, and three absorbers also are coupled in series, and all the other draw bails and flow direction of material are same as in figure 1.At this, only cold water is flowed to and cooling water flow to being illustrated, the flow direction of rest materials has just no longer repeated.Cold water flows to: deliver to the low-temperature air conditioner refrigeration area with water supply pump successively after three sections evaporimeters (3), flash evaporator (2), one section evaporimeter (1) divide three coolings to reach required low temperature from the cold water that the high-temperature air conditioner refrigeration area comes, send the high-temperature air conditioner refrigeration area again, cold-water return after twice intensification, get back to three sections evaporations again and steam (3), circulate again.Cooling water flow, divides high-temperature cooling waters after heating up for four times to deliver to the cooling tower cooling and reuses successively through one section absorber (4), two sections absorbers (5), three sections absorbers (6), condenser (10) to: the cooling water that comes from cooling tower.This scheme, about 23～24 ℃ of about 26～27 ℃ of room temperature of high-temperature air conditioner refrigeration area control, low-temperature air conditioner refrigeration area control room temperature, this is fully possible, not only reality but also feasible.The technology of this scheme compared with prior art, water supply pump energy efficient about 50%, comprehensive energy consumption is also saved about 50%, can be the bigger air conditioner refrigerating operating cost of colod-application family saving.
Claims (9)
1. a multistage absorption type refrigerating apparatus comprises generator, evaporimeter, absorber, condenser and supporting with it pump, heat exchanger, pipeline.It is characterized in that, it is by three generators, two or three evaporimeters, two or three absorbers, a condenser, four heat exchangers, and the pump that connects with it, valve, instrument, pipeline constitutes, adopt two sections or three sections absorption, promptly adopt triple effect to take place, two sections or three sections evaporations, the mode of two sections or three sections absorptions, two or three evaporimeters and two or three absorbers are installed in the same container, separate with dividing plate the centre, three generators are divided into high pressure, the middle pressure, low pressure generator, high pressure generator independently separately, middle generator and the low pressure generator of pressing can separate separately, also can be installed in the same container, the centre separates with dividing plate, and condenser and low pressure generator are with being contained in the container.Each section evaporimeter and each section absorber all are provided with the circulation infusion pump separately.
2, a kind of multistage absorption type refrigerating apparatus according to claim 1 is characterized in that, two or three evaporimeters are coupled in series, and two or three absorbers also are coupled in series.
3, a kind of multistage absorption type refrigerating apparatus according to claim 1, it is characterized in that, high pressure generator, middle pressure generator, low pressure generator adopt forward and crossfire journey, be that high pressure generator is connected with high pressure generator with low pressure generator parallel connection, middle pressure generator, perhaps adopt reverse and crossfire journey, press generator to connect with middle pressure generator promptly, perhaps adopt three generators flow process all in parallel with low pressure generator parallel connection, high pressure generator.
4, a kind of multistage absorption type refrigerating apparatus according to claim 1 is characterized in that the working medium that is adopted comprises lithium bromide, diethanol amine, triethanolamine.
5, a kind of multistage absorption type refrigerating apparatus according to claim 1, it is characterized in that, this device be two sections absorption, device comprises high pressure, middle pressure, low pressure triple effect generator, one section and two sections totally two evaporimeters, one section and two sections totally two absorbers, condenser altogether, first, second, third, fourth totally four heat exchangers, and the pump, valve, instrument, the pipeline that connect with it.
6, a kind of multistage absorption type refrigerating apparatus according to claim 1, it is characterized in that, this device be three sections absorption, colod-application family is divided into high-temperature air conditioner refrigeration area and low-temperature air conditioner refrigeration area or is divided into high temperature, middle temperature, low-temperature air conditioner refrigeration area, device comprises: high pressure, middle pressure, low pressure is the triple effect generator altogether, one section, two sections, three sections totally three evaporimeters, one section, two sections, three sections totally three absorbers, a condenser, first, second, third, fourth totally 4 heat exchangers, and the pump, valve, instrument, the pipeline that connect with it.
7, a kind of multistage absorption type refrigerating apparatus according to claim 1, it is characterized in that, the thermal source that high pressure generator adopted, when adopting lithium bromide to be working medium, adopt direct heat source or employing steam such as combustion gas, fuel oil, hot water etc. are thermal source indirectly, adopts diethanol amine, when triethanolamine is working medium, can only adopt thermal source indirectly such as steam, hot water.
8, a kind of multistage absorption type refrigerating apparatus according to claim 1, it is characterized in that, adopt two sections when absorption, its cold water flows to the cold water that comes from colod-application family and send colod-application family successively back to after twice cooling of flash evaporator, one section evaporimeter reaches required low temperature; Adopt three sections when absorption, the cold water that comes from colod-application family is sent colod-application family through three sections evaporimeters, flash evaporator, three coolings of one section evaporimeter back to after reaching required low temperature successively.
9, a kind of multistage absorption type refrigerating apparatus according to claim 1, it is characterized in that adopt two sections when absorption, its cooling water flow is to being, cooling water from cooling tower after one section absorber, two sections absorbers, condensers heat up for three times, is sent cooling tower back to successively; Adopt three sections when absorption, the cooling water that comes from cooling tower after one section absorber, two sections absorbers, three sections absorbers, condensers heat up for four times, is sent cooling tower back to successively.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB011336102A CN1158494C (en) | 2001-10-28 | 2001-10-28 | Multistage absorption type refrigerating apparatus |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB011336102A CN1158494C (en) | 2001-10-28 | 2001-10-28 | Multistage absorption type refrigerating apparatus |
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| CN1414326A true CN1414326A (en) | 2003-04-30 |
| CN1158494C CN1158494C (en) | 2004-07-21 |
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| CNB011336102A Expired - Fee Related CN1158494C (en) | 2001-10-28 | 2001-10-28 | Multistage absorption type refrigerating apparatus |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100344917C (en) * | 2006-04-05 | 2007-10-24 | 江苏双良空调设备股份有限公司 | Hot water two-stage multi-section lithium bromide absorption cold-water machine set |
| WO2012129743A1 (en) * | 2011-03-26 | 2012-10-04 | Li Huayu | Third-type generation-absorption system and third-type regenerative absorption heat pump |
| CN103175332A (en) * | 2013-04-07 | 2013-06-26 | 东南大学 | Two-stage absorption refrigeration circulation system based on double working pairs and refrigeration method thereof |
| CN104964477A (en) * | 2015-07-31 | 2015-10-07 | 上海缔森能源技术有限公司 | Multistage plate-type evaporation-absorption type refrigerating device and method |
| CN105485960A (en) * | 2016-01-08 | 2016-04-13 | 上海缔森能源技术有限公司 | Absorption refrigeration method and device of double-steam compression system |
| CN105650938A (en) * | 2016-01-08 | 2016-06-08 | 上海缔森能源技术有限公司 | Absorption refrigeration method and device for all-electric reuse of discharged heat |
-
2001
- 2001-10-28 CN CNB011336102A patent/CN1158494C/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100344917C (en) * | 2006-04-05 | 2007-10-24 | 江苏双良空调设备股份有限公司 | Hot water two-stage multi-section lithium bromide absorption cold-water machine set |
| WO2012129743A1 (en) * | 2011-03-26 | 2012-10-04 | Li Huayu | Third-type generation-absorption system and third-type regenerative absorption heat pump |
| CN103175332A (en) * | 2013-04-07 | 2013-06-26 | 东南大学 | Two-stage absorption refrigeration circulation system based on double working pairs and refrigeration method thereof |
| CN104964477A (en) * | 2015-07-31 | 2015-10-07 | 上海缔森能源技术有限公司 | Multistage plate-type evaporation-absorption type refrigerating device and method |
| CN105485960A (en) * | 2016-01-08 | 2016-04-13 | 上海缔森能源技术有限公司 | Absorption refrigeration method and device of double-steam compression system |
| CN105650938A (en) * | 2016-01-08 | 2016-06-08 | 上海缔森能源技术有限公司 | Absorption refrigeration method and device for all-electric reuse of discharged heat |
| CN105650938B (en) * | 2016-01-08 | 2018-01-09 | 上海缔森能源技术有限公司 | A kind of absorption-type refrigerating method and device of full electric power reuse discharge heat |
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