CN102032721A - Novel evaporator, novel condenser and adsorption refrigerator - Google Patents
Novel evaporator, novel condenser and adsorption refrigerator Download PDFInfo
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- CN102032721A CN102032721A CN2010105922553A CN201010592255A CN102032721A CN 102032721 A CN102032721 A CN 102032721A CN 2010105922553 A CN2010105922553 A CN 2010105922553A CN 201010592255 A CN201010592255 A CN 201010592255A CN 102032721 A CN102032721 A CN 102032721A
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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 discloses a novel evaporator, a novel condenser and an adsorption refrigerator. The evaporator and the condenser have an adsorption bed structure consisting of an absorbent and a heat exchanger. The refrigerator consisting of the novel evaporator and the novel condenser comprises a left side cavity and a right side cavity, wherein a first adsorption bed and a fourth adsorption bed are arranged in the left side cavity; a second adsorption bed and a third adsorption bed are arranged in the right side cavity; the other side of the fourth adsorption bed outside the left side cavity is connected to a second cooling water flow passage through a third valve; the other side of the first adsorption bed outside the left side cavity is connected to a driving heat source flow passage through a fourth valve; the other side of the third adsorption bed outside the right side cavity is connected to a freeze water flow passage through a fifth valve; the other side of the second adsorption bed outside the right side cavity is connected to a first cooling water flow passage through a sixth valve; and the evaporator and the condenser have the adsorption bed structure consisting of the absorbent and the heat exchanger. The refrigerant exists in a vapour state, so that the problems of unstable running and low refrigeration efficiency when the adsorption refrigerator is used for vibrating the liquid refrigerant in a moving system are solved; and the refrigerator has the characteristics of simple structure and the like, is easy to process and manufacture, and has important application value.
Description
Technical field
What the present invention relates to is a kind of novel evaporimeter and condenser and the adsorbent refrigerator be made up of novel evaporimeter and condenser, belongs to the adsorptive refrigeration technology field.
Background technology
Adsorptive refrigeration technology can utilize low temperature exhaust heat to drive refrigeration, and use environment amenable absorption working pair right as a kind of Refrigeration Technique of green, has energy-conservation and effect environmental protection, is paid close attention to widely.Adsorption refrigeration system can be utilized low-grade energies such as underground heat, solar energy, industrial exhaust heat and engine exhaust heat, alleviating energy crisis effectively.Adsorbent refrigerator is simple in structure, does not have moving component, can be used for places such as vibrations, inclination and rotation.Compare with Absorption Refrigerator, use more extensive.
Adsorbent refrigerator generally is made up of adsorbent bed, evaporimeter, condenser and pipeline, valve.Its process is: during the cooling adsorbent bed, the cold-producing medium of adsorbent bed absorption evaporator evaporation is finished adsorption process; During the heating adsorbent bed, make adsorbent bed resolve cold-producing medium, finish desorption process; The cold-producing medium that parses enters condenser, is condensed into liquid refrigerant, is back at last in the evaporimeter, finishes a cyclic process.In this process, there is liquid cold-producing medium in evaporimeter and the condenser.Though, adsorbent refrigerator can be used in sports centers such as vibrations, the picture on-board air conditioner, but the efficient of adsorbent refrigerator and stability are still waiting to improve, wherein the liquid refrigerant that exists in the device can produce vibrations along with motion, influence flow of refrigerant state and evaporation and condensation performance, cause adsorbent refrigerator in the sports center fluctuation of service, refrigerating efficiency is not high.
Patent of invention---truck tail gas adsorption refrigeration air conditioner for operator cabin, open day on January 7th, 2009, publication number CN101338954A, comprise generator, condenser, reservoir, choke valve, the air conditioner that contains the ammonia air-cooler, desorb check valve group, absorption check valve group, tail gas input sequencing valve group, cooling water input sequencing valve group, the PLC Programmable Logic Controller, the cooling water storage tank, water pump, cooler, and pipeline valve is communicated with into the loop, carry out programme-control with the PLC Programmable Logic Controller, utilize truck engine tail gas that one of generator is carried out heating desorption, utilize recirculated cooling water that all the other two generators are cooled off absorption, thereby form three generator adsorption refrigerating systems, and then the desorb and the sorption cycle of formation ammonia, and the kind of refrigeration cycle of ammonia drives the ammonia air-cooler to truck cap enforcement cooling.All there is liquid refrigerant in condenser, reservoir, the air conditioner that contains the ammonia air-cooler and the pipeline among the present invention, during the truck motion, the vibrations of liquid cold-producing medium influence the flow regime of cold-producing medium, and the stability of absorption type operation of air-conditioner is subjected to serious test.
Summary of the invention
The objective of the invention is to overcome above-mentioned the deficiencies in the prior art, the adsorbent refrigerator that a kind of novel evaporimeter and condenser is provided and constitutes by New Evaporator, condenser, evaporimeter and condenser are the adsorbent bed structure, solve to have liquid refrigerant in existing traditional evaporimeter, condenser and the pipeline and cause being applied in the sports center Effect on Performance to adsorbent refrigerator.Make that simultaneously adsorbent refrigerator is simple in structure, improve reliability of system operation and stability, help improving the refrigerating efficiency of system.
For realizing above purpose, the present invention has taked following technical scheme: a kind of novel evaporimeter and the adsorbent refrigerator of condenser and composition, and novel evaporimeter and condenser are for adopting the adsorbent bed structure of being made up of adsorbent and heat exchanger; The adsorbent refrigerator of forming by novel evaporimeter and condenser, two airtight left side cavitys and right side cavity about comprising, in the cavity of left side, be provided with first adsorbent bed, the 4th adsorbent bed that is connected with first adsorbent bed by first valve, in the cavity of right side, be provided with second adsorbent bed, the 3rd adsorbent bed that is connected with second adsorbent bed by second valve, described the 4th adsorbent bed opposite side, outside the cavity of left side, be connected to the second cooling water stream, perhaps be connected to the chilled water stream by the 7th valve by the 3rd valve; The described first adsorbent bed opposite side, outside the cavity of left side, be connected to the driving heat source stream, perhaps be connected to the first cooling water stream by the 8th valve by the 4th valve; Described the 3rd adsorbent bed opposite side, be connected to the chilled water stream by the 5th valve in that right-side cavity is external, perhaps be connected to the second cooling water stream by the 9th valve; The described second adsorbent bed opposite side, be connected to the first cooling water stream by the 6th valve in that right-side cavity is external, perhaps be connected to the driving heat source stream by the tenth valve.
Described evaporimeter is respectively the 3rd adsorbent bed, the 4th adsorbent bed with identical adsorbent material with condenser.
Has an identical adsorbent material in described first adsorbent bed, second adsorbent bed.
The adsorbent of described the 3rd adsorbent bed, the 4th adsorbent bed has different adsorbent materials with first adsorbent bed, second adsorbent bed.
Adsorbent in the described adsorbent bed and heat exchanger combination are filled type, painting type or cured type.
Described first adsorbent bed, second adsorbent bed alternately are connected with driving heat source stream, the first cooling water stream respectively, and the 3rd adsorbent bed, the 4th adsorbent bed alternately are connected with chilled water stream, the second cooling water stream respectively; Between described the 4th valve and first adsorbent bed, connect a branch road, this branch road other end is connected between the 6th valve and the first cooling water stream, connect a branch road between the 6th valve and second adsorbent bed, this branch road other end is connected between the 4th valve and the driving heat source stream; Between the 4th adsorbent bed and the 3rd valve, connect a branch road, this branch road other end is connected between the 5th valve and the chilled water stream, be connected with a branch road between the 3rd adsorbent bed and the 5th valve, this branch road other end is connected between the 3rd valve and the second cooling water stream.
Described first valve, second valve are the pressure check valve door.
Described adsorbent refrigerator is by control first adsorbent bed, the 4th adsorbent bed, and the temperature of second adsorbent bed, the 3rd adsorbent bed, adsorb or desorption process, make between the adsorbent bed of winning, the 4th adsorbent bed, and the pressure differential of each self-forming between second adsorbent bed, the 3rd adsorbent bed, promote the shuttling movement of the cold-producing medium of gaseous state, realize the refrigeration purpose.
The course of work of the present invention has two, and one is first adsorbent bed heating desorption process, second adsorbent bed cooling adsorption process, the 3rd adsorbent bed desorption process, the 4th adsorbent bed adsorption process; Two is first adsorbent bed cooling adsorption process, second adsorbent bed heating desorption process, the 3rd adsorbent bed adsorption process, the 4th adsorbent bed desorption process.
First adsorbent bed is connected with the driving heat source stream, when the 4th adsorbent bed is connected with the second cooling water stream, pressure in first adsorbent bed is greater than the pressure in the 4th adsorbent bed, the cold-producing medium of the first adsorbent bed desorption enters in the 4th adsorbent bed by first valve, first adsorbent bed is finished desorption process, the 4th adsorbent bed is finished adsorption process, and the 4th adsorbent bed is a condenser; Meanwhile, second adsorbent bed is connected with the first cooling water stream, when the 3rd adsorbent bed is connected with the chilled water stream, pressure in the 3rd adsorbent bed is greater than the pressure in second adsorbent bed, the cold-producing medium that the 3rd adsorbent bed desorption comes out enters in second adsorbent bed by second valve, second adsorbent bed is finished adsorption process, and the 3rd adsorbent bed is finished desorption process.In this process, the 3rd adsorbent bed is an evaporimeter, in the desorption process, because the existence of desorption heat realizes the purpose of freezing.
Second adsorbent bed is connected with the driving heat source stream, when the 3rd adsorbent bed is connected with the second cooling water stream, pressure in second adsorbent bed is greater than the pressure in the 3rd adsorbent bed, the cold-producing medium of the second adsorbent bed desorption enters in the 3rd adsorbent bed by second valve, second adsorbent bed is finished desorption process, the 3rd adsorbent bed is finished adsorption process, and the 3rd adsorbent bed is a condenser; Meanwhile, first adsorbent bed is connected with the cooling water stream, when the 4th adsorbent bed is connected with the chilled water stream, pressure in the 4th adsorbent bed is greater than the pressure in first adsorbent bed, the cold-producing medium of the 4th adsorbent bed desorption enters in first adsorbent bed by first valve, the 4th adsorbent bed is finished desorption process, and first adsorbent bed is finished adsorption process.In this process, the 4th adsorbent bed is an evaporimeter, in the desorption process, because the existence of desorption heat realizes the purpose of freezing.
During the heating of first adsorbent bed, first adsorbent bed connects the driving heat source stream, and second adsorbent bed connects the first cooling water stream, and the 3rd adsorbent bed connects the chilled water stream, and the 4th adsorbent bed connects the second cooling water stream; During the heating of second adsorbent bed, second adsorbent bed connects the driving heat source stream, and first adsorbent bed connects the first cooling water stream, and the 3rd adsorbent bed connects the second cooling water stream, and the 4th adsorbent bed connects the chilled water stream.By the switching of stream between first adsorbent bed, second adsorbent bed, the 3rd adsorbent bed, the 4th adsorbent bed, realize continuous cooling.
The present invention compared with prior art, have following advantage: beneficial effect of the present invention: evaporimeter and condenser adopt the adsorbent bed structure respectively, there is not liquid cold-producing medium in the described adsorbent refrigerator, can have effectively solved problems such as traditional adsorbent refrigerator fluctuation of service, refrigerating efficiency when kinematic system is used are not high.Have only the adsorbent bed structure in the described adsorbent refrigerator, simplified the structure of adsorbent refrigerator, help the processing and manufacturing in enormous quantities of adsorbent refrigerator.
Description of drawings
Fig. 1 is a concrete enforcement structural representation of the present utility model;
Fig. 2 is the adsorption process of zeolite and active carbon and the out-of-phase diagram of desorption process;
Description of reference numerals: 1-first adsorbent bed; 2-second adsorbent bed; 3-the 3rd adsorbent bed; 4-the 4th adsorbent bed; 7-left side cavity; 8-right side cavity; 5-first valve, 6-second valve, 23-the 3rd valve, 13-the 4th valve, 24-the 5th valve, 14-the 6th valve, 22-the 7th valve, 11-the 8th valve, 21-the 9th valve, 12-the tenth valve, 31-driving heat source stream; The 32-first cooling water stream; The 33-second cooling water stream; 34-chilled water stream.
The specific embodiment
Below in conjunction with the drawings and specific embodiments content of the present invention is described in further details.
Embodiment:
As shown in Figure 1, a kind of novel evaporimeter and the adsorbent refrigerator of condenser and composition comprise that evaporimeter and condenser are for adopting the adsorbent bed structure of being made up of adsorbent and heat exchanger; Two airtight left side cavitys 7 and right side cavity 8 about the adsorbent refrigerator of being made up of novel evaporimeter and condenser comprises, in left side cavity 7, be provided with first adsorbent bed 1, the 4th adsorbent bed 4 that is connected with first adsorbent bed 1 by first valve 5, in right side cavity 8, be provided with second adsorbent bed 2, the 3rd adsorbent bed 3 that is connected with second adsorbent bed 2 by second valve 6, the 4th adsorbent bed 4 opposite sides, outside left side cavity 7, be connected to the second cooling water stream 33, perhaps be connected to chilled water stream 34 by the 7th valve 22 by the 3rd valve 23; First adsorbent bed, 1 opposite side, outside left side cavity 7, be connected to driving heat source stream 31, perhaps be connected to the first cooling water stream 32 by the 8th valve 11 by the 4th valve 13; The 3rd adsorbent bed 3 opposite sides, outside right side cavity 8, be connected to chilled water stream 34, perhaps be connected to the second cooling water stream 33 by the 9th valve 21 by the 5th valve 24; Second adsorbent bed, 2 opposite sides, outside right side cavity 8, be connected to the first cooling water stream 32, perhaps be connected to driving heat source stream 31 by the tenth valve 12 by the 6th valve 14.Driving heat source stream 31, the first cooling water stream 32 link to each other with adsorbent bed 1, adsorbent bed 2 by the 8th valve 11, the tenth valve 12, the 4th valve 13, the 6th valve 14 respectively.The second cooling water stream 33, chilled water stream 34 link to each other with adsorbent bed 3, adsorbent bed 4 by the 9th valve 21, the 7th valve 22, the 3rd valve 23, the 5th valve 24 respectively.
Evaporimeter is respectively the 3rd adsorbent bed 3, the 4th adsorbent bed 4 with identical adsorbent material with condenser, and this adsorbent is a kind of active carbon in the present embodiment.
Has an identical adsorbent material in first adsorbent bed 1, second adsorbent bed 2.This kind adsorbent is a kind of zeolite in the present embodiment.
90 ℃ of hypothesis driven heat source temperatures, 35 ℃ of cooling water temperatures, 35 ℃ of chilled water temperatures.
When first adsorbent bed 1 connects driving heat source stream 31, the 4th adsorbent bed 4 connects the second cooling water stream 33, as shown in Figure 2, in first adsorbent bed 1 during 90 ℃ in zeolite desorption pressure be about 10kPa, the 4th adsorbent bed 4 interior 35 ℃ the time charcoal absorption pressure be about 5kPa, the pressure of first adsorbent bed 1 is greater than the pressure in the 4th adsorbent bed 4, and cold-producing medium enters the 4th adsorbent bed 4, the four adsorbent beds 4 from first adsorbent bed 1 and is equivalent to the condenser effect; Meanwhile, second adsorbent bed 2 connects the first cooling water stream 32, the 3rd adsorbent bed 3 connects chilled water stream 34, in second adsorbent bed 2 during 35 ℃ in zeolites adsorptive pressure less than 0.3kPa, in the 3rd adsorbent bed 3 during 35 ℃ of active carbons desorption pressure be about 7.1kPa, pressure in the 3rd adsorbent bed 3 is greater than the pressure in second adsorbent bed 2, cold-producing medium enters second adsorbent bed 2 from the 3rd adsorbent bed 3, and the part heat of cold-producing medium absorption refrigerating water during from the 3rd adsorbent bed 3 desorptions, chilled water is produced refrigeration, the 3rd adsorbent bed 3 is equivalent to the effect of evaporimeter, finishes a cyclic process.First adsorbent bed 1, second adsorbent bed 2 alternately connect the first cooling water stream 32, driving heat source stream 31; Meanwhile, the 3rd adsorbent bed 3, the 4th adsorbent bed 4 is the second connection cooling water stream 33 alternately, chilled water stream 34, realize the continuous cooling of adsorbent refrigerator, its concrete connected mode is: connect a branch road between the 4th valve 13 and first adsorbent bed 1, this branch road other end is connected between the 6th valve 14 and the first cooling water stream 32, between the 6th valve 14 and second adsorbent bed 2, connect a branch road, this branch road other end is connected between the 4th valve 13 and the driving heat source stream 31, between the 4th adsorbent bed 4 and the 3rd valve 23, connect a branch road, this branch road other end is connected between the 5th valve 24 and the chilled water stream 34, between the 3rd adsorbent bed 3 and the 5th valve 24, be connected with a branch road, this branch road other end is connected between the 3rd valve 23 and the second cooling water stream 33, be respectively equipped with the 8th valve 11 on the above-mentioned branch road, the tenth valve 12, the 9th valve 21, the seven valves 22.
The concrete course of work:
1. first adsorbent bed 1 heats desorption process, second adsorbent bed, 2 cooling adsorption processes, and the 3rd adsorbent bed 3 is an evaporimeter, the 4th adsorbent bed 4 is a condenser:
The 8th valve 11, the tenth valve 12 are closed, and the 4th valve 13, the 6th valve 14 are opened, and first adsorbent bed 1 is connected with driving heat source stream 31 by the 4th valve 13, and second adsorbent bed 2 is connected with the first cooling water stream 32 by the 6th valve 14; The 9th valve 21, the 7th valve 22 are closed, and the 3rd valve 23, the 5th valve 24 are opened, and the 3rd adsorbent bed 3 is connected with chilled water stream 34 by the 5th valve 24, and the 4th adsorbent bed 4 is connected with the second cooling water stream 33 by the 3rd valve 23.Pressure in first adsorbent bed 1 is greater than the pressure in the 4th adsorbent bed 4, the cold-producing medium of first adsorbent bed, 1 desorption enters in the 4th adsorbent bed 4 by first valve 5, first adsorbent bed 1 is finished desorption process, and the 4th adsorbent bed 4 is finished adsorption process, and the 4th adsorbent bed 4 is a condenser; Meanwhile, the pressure in the 3rd adsorbent bed 3 is greater than the pressure in second adsorbent bed 2, and the cold-producing medium that the 3rd adsorbent bed 3 desorptions come out enters in second adsorbent bed 2 by second valve 6, and second adsorbent bed 2 is finished adsorption process, and the 3rd adsorbent bed 3 is finished desorption process.In this process, the 3rd adsorbent bed 3 is an evaporimeter, in the desorption process, because the existence of desorption heat realizes the purpose of freezing.
2, first adsorbent bed, 1 cooling adsorption process, second adsorbent bed, 2 heating desorption processes, the 3rd adsorbent bed 3 is a condenser, the 4th adsorbent bed 4 is an evaporimeter:
The 4th valve 13, the 6th valve 14 are closed, and the 8th valve 11, the tenth valve 12 are opened, and first adsorbent bed 1 is connected with the first cooling water stream 32 by the 8th valve 11, and second adsorbent bed 2 is connected with driving heat source stream 31 by the tenth valve 12; The 3rd valve 23, the 5th valve 24 are closed, and the 9th valve 21, the 7th valve 22 are opened, and the 3rd adsorbent bed 3 is connected with the second cooling water stream 33 by the 9th valve 21, and the 4th adsorbent bed 4 is connected with chilled water stream 34 by the 7th valve 22.Pressure in second adsorbent bed 2 is greater than the pressure in the 3rd adsorbent bed 3, the cold-producing medium of second adsorbent bed, 2 desorptions enters in the 3rd adsorbent bed 3 by second valve 6, second adsorbent bed 2 is finished desorption process, and the 3rd adsorbent bed 3 is finished adsorption process, and the 3rd adsorbent bed 3 is a condenser; Meanwhile, the pressure in the 4th adsorbent bed 4 is greater than the pressure in first adsorbent bed 1, and the cold-producing medium of the 4th adsorbent bed 4 desorptions enters in first adsorbent bed 1 by first valve 5, and the 4th adsorbent bed 4 is finished desorption process, and first adsorbent bed 1 is finished adsorption process.In this process, the 4th adsorbent bed 4 is an evaporimeter, in the desorption process, because the existence of desorption heat realizes the purpose of freezing.
Above-listed detailed description is at the specifying of possible embodiments of the present invention, and this embodiment is not in order to limiting claim of the present invention, and the equivalence that all the present invention of disengaging do is implemented or change, all should be contained in the claim of this case.
Claims (7)
1. novel evaporimeter and condenser and adsorbent refrigerator is characterized in that: described evaporimeter and condenser are for adopting the adsorbent bed structure of being made up of adsorbent and heat exchanger; Two airtight left side cavitys (7) and right side cavity (8) about described adsorbent refrigerator comprises, in left side cavity (7), be provided with first adsorbent bed (1), the 4th adsorbent bed (4) that is connected with first adsorbent bed (1) by first valve (5), in right side cavity (8), be provided with second adsorbent bed (2), the 3rd adsorbent bed (3) that is connected with second adsorbent bed (2) by second valve (6), described the 4th adsorbent bed (4) opposite side, outside left side cavity (7), be connected to the second cooling water stream (33), perhaps be connected to chilled water stream (34) by the 7th valve (22) by the 3rd valve (23); Described first adsorbent bed (1) opposite side, outside left side cavity (7), be connected to driving heat source stream (31), perhaps be connected to the first cooling water stream (32) by the 8th valve (11) by the 4th valve (13); Described the 3rd adsorbent bed (3) opposite side, outside right side cavity (8), be connected to chilled water stream (34), perhaps be connected to the second cooling water stream (33) by the 9th valve (21) by the 5th valve (24); Described second adsorbent bed (2) opposite side, outside right side cavity (8), be connected to the first cooling water stream (32), perhaps be connected to driving heat source stream (31) by the tenth valve (12) by the 6th valve (14).
2. novel evaporimeter as claimed in claim 1 and condenser and adsorbent refrigerator is characterized in that: described evaporimeter is respectively the 3rd adsorbent bed (3), the 4th adsorbent bed (4) with identical adsorbent material with condenser.
3. novel evaporimeter as claimed in claim 1 and condenser and adsorbent refrigerator is characterized in that: have identical adsorbent material in described first adsorbent bed (1), second adsorbent bed (2).
4. novel evaporimeter as claimed in claim 1 and condenser and adsorbent refrigerator is characterized in that: the adsorbent of described the 3rd adsorbent bed (3), the 4th adsorbent bed (4) has different adsorbent materials with first adsorbent bed (1), second adsorbent bed (2).
5. novel evaporimeter as claimed in claim 1 and condenser and adsorbent refrigerator is characterized in that: adsorbent in the described adsorbent bed and heat exchanger combination are filled type, painting type or cured type.
6. novel evaporimeter as claimed in claim 1 and condenser and adsorbent refrigerator, it is characterized in that: described first adsorbent bed (1), second adsorbent bed (2) alternately are connected with driving heat source stream (31), the first cooling water stream (32) respectively, and the 3rd adsorbent bed (3), the 4th adsorbent bed (4) alternately are connected with chilled water stream (34), the second cooling water stream (33) respectively; Between described the 4th valve (13) and first adsorbent bed (1), connect a branch road, this branch road other end is connected between the 6th valve (14) and the first cooling water stream (32), connect a branch road between the 6th valve (14) and second adsorbent bed (2), this branch road other end is connected between the 4th valve (13) and the driving heat source stream (31); Between the 4th adsorbent bed (4) and the 3rd valve (23), connect a branch road, this branch road other end is connected between the 5th valve (24) and the chilled water stream (34), be connected with a branch road between the 3rd adsorbent bed (3) and the 5th valve (24), this branch road other end is connected between the 3rd valve (23) and the second cooling water stream (33).
7. novel evaporimeter as claimed in claim 1 and condenser and adsorbent refrigerator is characterized in that: described first valve (5), second valve (6) are the pressure check valve door.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010105922553A CN102032721B (en) | 2010-12-16 | 2010-12-16 | Adsorption refrigerator including evaporator and condenser |
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| Application Number | Priority Date | Filing Date | Title |
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| CN2010105922553A CN102032721B (en) | 2010-12-16 | 2010-12-16 | Adsorption refrigerator including evaporator and condenser |
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| CN102032721A true CN102032721A (en) | 2011-04-27 |
| CN102032721B CN102032721B (en) | 2013-07-31 |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107543332A (en) * | 2017-10-09 | 2018-01-05 | 广州市香港科大霍英东研究院 | A kind of close-coupled absorbing refrigeration system |
| CN108413643A (en) * | 2017-02-09 | 2018-08-17 | 九星E&C | For the triple valve of independent control flow path including its adsorption refrigerating device and adsorption refrigeration system |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4183734A (en) * | 1977-06-01 | 1980-01-15 | Cjb Developments Limited | Adsorption heat pump |
| CN2531965Y (en) * | 2001-12-14 | 2003-01-22 | 殷柏青 | Air conditioner utilizing car tail gas |
| EP1964601A2 (en) * | 2007-02-26 | 2008-09-03 | Hamilton Sundstrand Corporation | Thermally linked molecular sieve beds for CO2 removal |
| CN101482342A (en) * | 2008-01-09 | 2009-07-15 | 财团法人工业技术研究院 | Solid adsorption type heat pump |
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2010
- 2010-12-16 CN CN2010105922553A patent/CN102032721B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4183734A (en) * | 1977-06-01 | 1980-01-15 | Cjb Developments Limited | Adsorption heat pump |
| CN2531965Y (en) * | 2001-12-14 | 2003-01-22 | 殷柏青 | Air conditioner utilizing car tail gas |
| EP1964601A2 (en) * | 2007-02-26 | 2008-09-03 | Hamilton Sundstrand Corporation | Thermally linked molecular sieve beds for CO2 removal |
| CN101482342A (en) * | 2008-01-09 | 2009-07-15 | 财团法人工业技术研究院 | Solid adsorption type heat pump |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108413643A (en) * | 2017-02-09 | 2018-08-17 | 九星E&C | For the triple valve of independent control flow path including its adsorption refrigerating device and adsorption refrigeration system |
| CN107543332A (en) * | 2017-10-09 | 2018-01-05 | 广州市香港科大霍英东研究院 | A kind of close-coupled absorbing refrigeration system |
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|---|---|
| CN102032721B (en) | 2013-07-31 |
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