CN1122164C - Dual-generator adsorption refrigerating system - Google Patents
Dual-generator adsorption refrigerating system Download PDFInfo
- Publication number
- CN1122164C CN1122164C CN99115216A CN99115216A CN1122164C CN 1122164 C CN1122164 C CN 1122164C CN 99115216 A CN99115216 A CN 99115216A CN 99115216 A CN99115216 A CN 99115216A CN 1122164 C CN1122164 C CN 1122164C
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- Prior art keywords
- generator
- condenser
- communicated
- refrigeration
- stop valve
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- Expired - Fee Related
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- 238000001179 sorption measurement Methods 0.000 title claims abstract description 10
- 239000007788 liquid Substances 0.000 claims abstract description 20
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims abstract description 13
- 239000003507 refrigerant Substances 0.000 claims description 20
- 239000002826 coolant Substances 0.000 claims description 8
- 229910021529 ammonia Inorganic materials 0.000 claims description 6
- 238000005057 refrigeration Methods 0.000 abstract description 23
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 9
- 239000003463 adsorbent Substances 0.000 description 7
- 238000001816 cooling Methods 0.000 description 7
- 238000009413 insulation Methods 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 3
- 210000005056 cell body Anatomy 0.000 description 3
- 238000003795 desorption Methods 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 238000007789 sealing Methods 0.000 description 3
- 229910001628 calcium chloride Inorganic materials 0.000 description 2
- 239000001110 calcium chloride Substances 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- -1 compound calcium chloride Chemical class 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 235000013332 fish product Nutrition 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
Images
Classifications
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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
-
- 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]
-
- 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
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Abstract
The present invention discloses an adsorption refrigerating system which can realize continuous refrigeration and has stable refrigeration temperature. The present invention is provided with a condenser (5), wherein a liquid storage barrel (4) of refrigeration agents and liquid ammonia and an evaporator (2) are arranged in the condenser (5); refrigeration agent guide pipes of a generator (8) and a generator (9) are communicated with the refrigeration agent inlet end of the condenser (5) through a stop valve (7) and a stop valve (6); the refrigeration agent outlet end of the condenser (5) are communicated with the liquid inlet of the liquid storage barrel (4); the liquid outlet of the liquid storage barrel (4) is communicated with the liquid inlet of the evaporator (2) through a throttling valve (3); the refrigeration agent outlet end of the evaporator (2) is respectively connected with the refrigeration agent guide pipes of the generator (9) and the generator (8) through a stop valve (10) and a stop valve (11).
Description
The present invention relates to refrigeration system, further be meant adsorption refrigeration system.
Traditional adsorption refrigeration system is come out for many years.It is mainly connected to form by separate unit generator and condenser, evaporimeter, makees adsorbent with calcium chloride usually, makees cold-producing medium with ammonia.When adding heater, the cold-producing medium that adsorbent absorbed wherein discharges with the steam state form, is that liquid state enters evaporimeter through condenser condenses; Stop to add heater, then described adsorbent just absorbs the liquid refrigerant in the evaporimeter with steam state, and cold-producing medium is evaporated in steam state and the absorbed process by liquid state in the evaporimeter, and the absorbing environmental heat is realized refrigeration.Not freezing when read procedure essence is heating and freeze when stopping to heat, is the batch (-type) refrigeration.For overcoming described technological deficiency, development person once adopted the many group said apparatus and the refrigeration that makes it to hocket in same refrigeration plant, with alleviation unstable temperature problem, but did not break through the limitation that system's batch (-type) freezes yet, and refrigeration is still undesirable.
The objective of the invention is, design dual-generator adsorption refrigerating system, can achieve continuous cooling, to obtain stable cryogenic temperature, and have the characteristics of structure tube list, dependable performance, make the environmental type adsorb refrigerating device that provides practicability become possibility thus.
Technical scheme of the present invention is, described dual-generator adsorption refrigerating system comprises generator, condenser, in the surge drum and the evaporimeter of cold-producing medium liquefied ammonia are arranged, its design feature is, first, the coolant conduits of second generator is through corresponding first, second stop valve is communicated with the refrigerant inlet end of condenser, the refrigerant outlet end of condenser is communicated with the inlet of surge drum, the liquid outlet of surge drum is communicated with the inlet of evaporimeter through choke valve, and the refrigerant outlet end of evaporimeter is through the 3rd, the 4th stop valve is respectively with first, the described coolant conduits of second generator is communicated with.
The present invention is actually each the related work unit of absorbing refrigeration system that utilizes prior art, double-generator (i.e. two generators) is set on this basis and through specific connection so that it can realize that continuous cooling finishes, double-generator of the present invention is meant two (platform) generators that the duty of its absorption or desorption is separate.Below in conjunction with accompanying drawing the present invention is made and to further specify.
Description of drawings:
Fig. 1 is a system construction drawing of the present invention;
Fig. 2 is the ice build-up tank of embodiment and the sectional view of evaporation structure;
Fig. 3 is the condenser of embodiment and the sectional view of surge drum,
Fig. 4 and Fig. 5 are respectively the axial and radial section structures of a generator.
In described accompanying drawing:
1-refrigeration area 2-evaporimeter 3-choke valve
4-surge drum 5-condenser 6,7,10,11-stop valve
8, the box ice build-up tank cell body of 9-generator 13-14-case lid
15-fin 16-cylindrical shell 17-refrigerant outlet end
The heat insulation cylindrical shell 20-of 18-inlet 19-inlet
21-liquid outlet 22-refrigerant outlet end 23-water inlet
24-spiral coil 25-refrigerant inlet end 26-delivery port
27-water leg 28-connector 29-suspension ring
30-porous plate 31-exhaust duct 32-shell
33-admitting pipe joint 34-watering transverse tube 35-coolant conduits
Pipe 38-core pipe in the 36-titting water outlet 37-
39-adsorbent 40-ring flange
As shown in Figure 1, the present invention includes generator (8,9), condenser (5), in the surge drum (4) and the evaporimeter (2) of cold-producing medium liquefied ammonia are arranged, its design feature is, first, second generator (8,9) coolant conduits is through corresponding first, second stop valve (6,7) the refrigerant inlet end of same condenser (5) is communicated with, the inlet of the same surge drum of refrigerant outlet end (4) of condenser (5) is communicated with, and the liquid outlet of surge drum (4) is communicated with through the inlet of choke valve (3) with evaporimeter (2), and the refrigerant outlet end of evaporimeter (2) is through the 3rd, the 4th stop valve (10,11) respectively with first, second generator (8,9) described coolant conduits is communicated with.Described connection adopts conventional communicating pipe to realize.Described first, second generator (8,9) is meant the separate generator of its duty in two courses of work, and single generator (8) or (9) can be made up of a plurality of generator units or a generator unit.(8) or (9) can form by a plurality of generator units or a generator unit.
Operation principle of the present invention is (referring to Fig. 1), when cooling off generator (8) simultaneously when adding heater (9), open stop valve (6) (11) and close stop valve (7) (10) this moment, adsorbent in the generator (9) just discharges (promptly producing " desorption " effect) with adsorbed cold-producing medium with the steam state form, its vaporized refrigerant enters through stop valve (6) and enters surge drum (4) again after condenser (5) is condensed into liquid state, and the liquid refrigerant in this surge drum (4) is supplemented in the evaporimeter (2) through choke valve (3); Meanwhile, owing to be subjected to cooling effect, adsorbent produces suction-operated to the cold-producing medium in the system in the generator (8), promptly this generator (8) adsorbs with the form of steam state the liquid refrigerant in the evaporimeter (2) through stop valve (11), liquid refrigerant in the evaporimeter (2) is become by liquid state and absorbs a large amount of heat of surrounding environment in the process of steam state, realizes refrigeration; When " desorption " of generator (9) finished and " absorption " of generator (8) reaches capacity, then close stop valve (6) (11) and open stop valve (7) (10), add heater (8) this moment and cool off generator (9) simultaneously, then the process of refrigerastion of system is identical with above-mentioned process of refrigerastion principle, so alternately, realized the continuous cooling of system, promptly realized the peculiar kind of refrigeration cycle of compression refrigerating system---Carnot cycle, this is absorbing refrigeration system breakthrough technically.Surge drum (4) plays the effect of cold-producing medium balance in the regulating system.Described choke valve can be called heating power expansion valve again from the action principle angle, and it plays the effect of high pressure liquid refrigerant being carried out throttling step-down (refrigerant flow and the pressure of evaporimeter is sent in adjustment), and its operation principle is the conventional principles of prior art.
As known from the above, the present invention is a kind of dual-generator adsorption refrigerating system, system has realized continuous cooling, and has characteristics simple in structure, dependable performance, makes to produce the practicability adsorption refrigerating device (Green Product of no freon) with stable cryogenic temperature and become possibility.
Embodiment: a kind of seagoing fishing vessel diesel engine vent gas ice machine that goes out according to Fig. 1 and said system structural design, it comprises ice build-up tank, surge drum, condenser and generator.Fig. 2 is the practical structures of ice build-up tank, it has heat insulation box cell body (13) and case lid (14), cell body (13) is equipped with evaporimeter (2), this evaporimeter (2) is connected in series the connection formation successively by cylindrical shell (16) head and the tail of some sealings, and inlet (18) is set and at the other end port of export (17) is set at the one end, each cylindrical shell (16) outer surface is equipped with the fin (15) that is beneficial to heat conduction; Referring to Fig. 3, (210 form surge drum (4) by heat insulation cylindrical shell (19) and inlet (20) and liquid outlet; Again referring to Fig. 3, described condenser (5) is made up of water leg (27) and the spiral coil (24) that is loaded on wherein, water leg (27) has top delivery port (26) and lower water inlet (23), and spiral coil (24) has the refrigerant inlet end (25) and the port of export (22); Referring to Fig. 4 and Fig. 5, the structure of described generator (8) or (9) is, exhaust duct (31) perforation is arranged in the shell (32) and on pipe (31), interior pipe (37) is housed, be equipped with some core pipes (38) in the cavity between exhaust duct (31) and the interior pipe (37) and be placed with compound calcium chloride adsorbent, have some small through hole on core pipe (38) tube wall, each core pipe (38) one end sealing and the other end is an opening end, its cavity at this opening end place is communicated with coolant conduits (35), the porous watering transverse tube (34) that the admitting pipe joint (33) on shell (32) top is located on interior pipe (37) top is connected, titting water outlet (36) is arranged at shell (32) bottom, above-mentioned each member is coupled together the system circuit that constitutes sealing by Fig. 1 and aforementioned system structure, and can be on system pipeline the setting pressure table with the observing system working condition.System adopts ammonia to make cold-producing medium (filling liquefied ammonia in the surge drum (4)).Because the absorption refrigeration cycle of single generator of the present invention (8) or (9) is about half an hour, so described stop valve (6) (7) (10) (11) can adopt existing hand-operated valve, also can adopt the control stop valve of prior aries such as pneumatic operated valve or electric-air valve.The heat insulation structural of described ice build-up tank and surge drum can adopt the heat insulation structural of prior art such as filling foamed plastics between two-layer tank wall.During on-the-spot the installation, can will link to each other with the diesel engine of fishing vessel tail gas discharging pipe again after (9) two parallel connections of generator shown in Figure 4 (8), make the tail gas can only be with a commutation valve, the water inlet (23) of condenser (5) and generator (8) (9) or admitting pipe joint (33) are connected to the cooling water water source tube through corresponding water valve get final product work generator heating and convertible.Generator (8) (9) and condenser (5) also can adopt mode air-cooled or cooling naturally to cool off.The present invention accepts the heat energy of 200 horsepower diesel offgas duct, and refrigerating capacity is 10000-15000KCal/h, ice-making capacity 1-3T/24h, the maximum working pressure 11kg/cm of system
2, cryogenic temperature reaches-13 ℃.Made ice cube replaces the traditional work mode that the ice of fishing boat band in the last hundred years goes fishing on the sea, and efficiently solves the fishing boat refrigeration needs fresh-keeping to fish product, greatly reduces the fishing production cost, do not influence the power output of diesel engine again, do not increase its oil consumption, saved the energy, non-environmental-pollution.
Claims (1)
1, a kind of dual-generator adsorption refrigerating system, comprise generator (8,9), condenser (5), in the surge drum (4) and the evaporimeter (2) of cold-producing medium liquefied ammonia are arranged, it is characterized in that, first, second generator (8,9) coolant conduits is through corresponding first, second stop valve (6,7) the refrigerant inlet end of same condenser (5) is communicated with, the inlet of the same surge drum of refrigerant outlet end (4) of condenser (5) is communicated with, and the liquid outlet of surge drum (4) is communicated with through the inlet of choke valve (3) with evaporimeter (2), and the refrigerant outlet end of evaporimeter (2) is through the 3rd, the 4th stop valve (10,11) respectively with first, second generator (8,9) described coolant conduits is communicated with.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN99115216A CN1122164C (en) | 1999-01-13 | 1999-01-13 | Dual-generator adsorption refrigerating system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN99115216A CN1122164C (en) | 1999-01-13 | 1999-01-13 | Dual-generator adsorption refrigerating system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1260467A CN1260467A (en) | 2000-07-19 |
| CN1122164C true CN1122164C (en) | 2003-09-24 |
Family
ID=5278220
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN99115216A Expired - Fee Related CN1122164C (en) | 1999-01-13 | 1999-01-13 | Dual-generator adsorption refrigerating system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1122164C (en) |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1300542C (en) * | 2004-05-13 | 2007-02-14 | 上海交通大学 | Waste heat driven composite alternating heat pipe generator |
| CN100523653C (en) * | 2007-08-27 | 2009-08-05 | 武汉云鹤定宇制冷科技有限公司 | Adsorption refrigerating system with two and above generators |
| CN100516717C (en) * | 2007-08-27 | 2009-07-22 | 武汉云鹤定宇制冷科技有限公司 | Oil gas field light hydrocarbon recovery device |
| CN106516434A (en) * | 2016-12-26 | 2017-03-22 | 天津商业大学 | Adsorption type portable refrigeration transportation box |
| CN106949661A (en) * | 2017-05-09 | 2017-07-14 | 上海海洋大学 | A kind of Novel Adsorption Cooling system |
-
1999
- 1999-01-13 CN CN99115216A patent/CN1122164C/en not_active Expired - Fee Related
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| Publication number | Publication date |
|---|---|
| CN1260467A (en) | 2000-07-19 |
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| Date | Code | Title | Description |
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| C06 | Publication | ||
| PB01 | Publication | ||
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| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
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| ASS | Succession or assignment of patent right |
Owner name: WUHAN YUNHE DINGYU REFRIGERATION TECHNOLOGY CO., Free format text: FORMER OWNER: LI DINGYU Effective date: 20040806 |
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| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20040806 Address after: 430200 Hubei Province, Wuhan city Wuchang District No. 3 cave street. Patentee after: Wuhan Yunhe Dingyu Refrigeration Technology Co., Ltd. Address before: 410006 Hunan province Changsha City three building 4 unit 7 moon lake No. 507 Patentee before: Li Dingyu |
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| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20030924 Termination date: 20130113 |