CN1570535A - Waste heat driven composite alternating heat pipe generator - Google Patents
Waste heat driven composite alternating heat pipe generator Download PDFInfo
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- CN1570535A CN1570535A CN 200410018291 CN200410018291A CN1570535A CN 1570535 A CN1570535 A CN 1570535A CN 200410018291 CN200410018291 CN 200410018291 CN 200410018291 A CN200410018291 A CN 200410018291A CN 1570535 A CN1570535 A CN 1570535A
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Abstract
The invention relates to a kind of generator droved by remnant heat energy with compound and pulsant heating-pipeline, being used in the field of adsorbent ice-making on the boat. The smoke and gas heating pipeline is located at the bottom of the steam boiler, and the out space of the pipeline forms the steam generator. The segment for steam-regenerating is connected to the katabatic segment of heating-pipeline, linking to the adsorbent platform. The battery valve of heating-pipeline is installed between the katabatic segment of heating-pipeline and the heating pipeline. The katabatic segment of heating-pipeline is connected to the heating pipeline. The adsorbent segment is located in the inside of the adsorbent platform. The pipeline for ammonia gas is weld to the adsorbent segment. Linking to the pipeline of ammonia medium. The export of adsorb and segregating ammonia is the external equipment of the ammonia pipeline. The adsorbent is in the adsorbent segment. Cold-producing tube for seawater is located in the adsorbent segment, and the pipeline for seawater is connected to it. The entrance and output for seawater is linking to the Cold-producing tube via seawater pipeline. The bottom of the pressure-controlling room is connected to the bottom of the steam generator.
Description
Technical field
What the present invention relates to is a kind of composite alternating heat pipe generator that is used for ice making peculiar to vessel field, specifically is the composite alternating heat pipe generator that a kind of waste heat drives.
Background technology
At present, the coastal middle-size and small-size fishing boat of China is mostly fresh-keeping based on iced storage, and mechanical refrigeration is fresh-keeping to be auxilliary.Therefore, the fishing boat refrigeration machine is the equipment that current medium and small fishing boat presses for equipment, develops the steam compression type refrigerating mode that still concentrates on.Meanwhile, the diesel engine on the fishing boat has 30% heat to enter atmosphere and waste from tail gas approximately.If can utilize this part waste heat to drive adsorption refrigeration system, can not increase any oil consumption of diesel engine, only reclaim its using waste heat from tail gas and realize ice making, satisfy fisherman's demand.
It is cold-producing medium that absorption refrigeration equipment peculiar to vessel mainly adopts water, ammonia and methyl alcohol, and wherein adopting water, methyl alcohol is that the system of cold-producing medium generally adopts physical absorbent, relatively with to adopt chemosorbent-ammonia be working medium for system, refrigerating capacity is less than normal.And, because ammonia and copper product, have incompatibility between seawater and the steel material for ammonia system, be that the system of cold-producing medium generally can not adopt seawater directly to cool off so adopt ammonia at present, otherwise can have serious etching problem.Fishing boat absorption refrigeration equipment, currently used adsorbent bed form mostly is unit tubular type and shell-tube type.
Find number of patent application by literature search: 200310108923.0, name is called: composite alternating heat pipe adsorbent bed, it is cold-producing medium that this patent adopts ammonia, calcium chloride is adsorbent.The heating and the methods for cooling that change adsorbent bed adopt the composite alternating heat pipe, but because the heating part of its adsorbent bed adopts the direct opposite heat tube of flue gas to heat, when adsorbent bed cools off, gas fume valve is closed, the heat pipe bringing-up section of adsorbent bed is to be in the alternating hot and cold state, flue gas can condense on the heat pipe bringing-up section pipeline of adsorbent bed like this, forms acid etching.This system is under the state of cooling on the other hand, the valve closing of control heat pipe bringing-up section, like this because the heat pipe of adsorbent bed part belongs to two different confined spaces respectively with the heat pipe of heat pipe bringing-up section, also there is certain difference in two-part temperature simultaneously, so the pressure of heat pipe bringing-up section will be higher than the pressure of inside heat pipe in the adsorbent bed, is unfavorable for the safe operation of system like this.
Summary of the invention
The objective of the invention is to overcome above-mentioned the deficiencies in the prior art, the composite alternating heat pipe generator that provides a kind of waste heat to drive makes it solve the flue gas corrosion problem of heat pipe bringing-up section in the existing composite alternating heat pipe adsorbent bed, improves reliability of system operation simultaneously.
The present invention is that following technical scheme realizes, the present invention includes: flue gas heated type steam boiler, flue gas heating pipe line, steam generator, steam regenerator/heat pipe bringing-up section, heat pipe magnetic valve, heat pipe descending branch, heat-pipe working medium section, ammonia adsorption/desorption mouth, ammonia mass transfer pipeline, ammonia pipeline, adsorbent bed, adsorb unit pipe, adsorbent, sea water condenser, heat pipe condenser section, seawaterline, seawater valve, sea intake, seawer outlet, pressure control air storage chamber.Its connected mode is: the flue gas heating pipe line is positioned at the bottom of flue gas heated type steam boiler, the inner logical flue gas of pipe, flue gas heating pipe line space outerpace constitutes steam generator, employing water is medium, steam regenerator/heat pipe bringing-up section bottom links to each other with the heat pipe descending branch by the heat pipe magnetic valve, insert the upper space of flue gas heating pipe line then, the top by flue gas heating steam boiler picks out again, inserts the inner space at adsorbent bed middle part at last again by the outer wall of adsorbent bed.The heat pipe magnetic valve is connected between the heat pipe descending branch and steam regenerator/heat pipe bringing-up section of adsorbent bed bottom, the heat pipe descending branch is connected the bottom of adsorbent bed, be connected with the heat-pipe working medium section of adsorbent bed inside, adsorb unit pipe is positioned at the lower space of adsorbent bed inside, adopt steel pipe, ammonia mass transfer pipeline is positioned at the middle part of adsorb unit pipe, adopt screen casing, the ammonia pipeline is welded on the top and bottom center of adsorb unit pipe, communicate with the ammonia mass transfer pipeline of adsorb unit pipe inside, ammonia adsorption/desorption mouth is the outlet of ammonia pipeline in the adsorbent bed outside.Adsorbent is filled within the adsorb unit pipe, is positioned at the space outerpace of ammonia mass transfer pipeline.Sea water condenser is positioned at the upper space of the inner adsorb unit pipe of adsorbent bed.Seawaterline is connected with the two ends of sea water condenser, and sea intake is connected with sea water condenser by seawaterline respectively with seawer outlet, and the seawater valve is connected on the seawaterline at sea intake place.The lower space of the outside of adsorb unit pipe and sea water condenser constitutes the heat-pipe working medium section in the adsorbent bed, and the space on sea water condenser outside and adsorb unit pipe top constitutes heat pipe condenser section in the adsorbent bed.The bottom space of steam generator is inserted in pressure control air storage chamber bottom, and wherein adopting water is liquid medium, and the top of water adopts nitrogen to come pressure control.
In the sea water condenser pipe is seawater, and pipe is outer to be the working media of heat pipe, i.e. steam.Heat of adsorption is taken away in the evaporation of the outer wall of water vapour adsorb unit pipe in the heat-pipe working medium section, then at the surface condensation of sea water condenser.Sea water condenser so can adopt copper material, so promptly can prevent seawater corrosion owing to being by two different spaces of the airtight one-tenth of ammonia pipeline with the ammonia space of adsorb unit pipe inside, also can not have the etching problem of ammonia to copper product.The steam that the thermal recovery steam regenerator/the heat pipe bringing-up section is produced that adds of adsorb unit pipe heats, steam regenerator/heat pipe bringing-up section then heats by the steam of steam generator, can avoid the etching problem that is produced in the direct heating process of flue gas opposite heat tube bringing-up section like this.Owing to adopted this novel mode of heating, flue gas heated type steam boiler is in the adsorb unit pipe cooling procedure, flue gas can not switch, only close the heat pipe magnetic valve of adsorbent bed bottom, the limited gas evaporation of steam regenerator/heat pipe bringing-up section inside can not cause very big influence to the cooling of adsorb unit pipe like this.And because steam regenerator/heat pipe bringing-up section is connected with the heat-pipe working medium section of adsorbent bed inside, so the pressure balance at heat pipe magnetic valve two ends, this helps the reliability of system works.
The work of this generator mainly comprises two processes, and one is the heating desorption process.In the heating desorption process, under the flue gas heat effect of flue gas pipeline, steam raising in the steam generator, this moment adsorbent bed the seawater valve closing, the heat pipe magnetic valve is opened, under the Steam Heating effect in steam generator, aqueous medium evaporation in steam regenerator/heat pipe bringing-up section, the outer wall condensation of adsorb unit pipe in the heat-pipe working medium section, for adsorb unit pipe provides heat and the temperature of adsorb unit pipe is risen, when the temperature of adsorbent in the unit pipes rise to can the temperature of desorb after, the cold-producing medium in the adsorbent desorbs from adsorbent, finishes desorption process.Another course of work of adsorbent bed is the cooling adsorption process.In the cooling adsorption process, the heat pipe closed electromagnetic valve, the seawater valve opening, the aqueous medium of heat-pipe working medium section is in the outer wall evaporation of adsorb unit pipe, take away the heat of adsorption of the inner adsorbent of adsorb unit pipe, sea water condenser cools off water vapour under the cooling effect of seawater, water recovery Cheng Shuihou flows back to the heat-pipe working medium section again, repeating above process cools off the adsorbent of adsorb unit pipe inside, after the temperature of adsorbent drops to adsorption temp, cold-producing medium begins to be adsorbed in the adsorbent, finishes adsorption process.
The characteristics of this generator also are to utilize a steam generator to finish the design of multibed system, can be installed in the steam regenerator of two or many generators the upper space of same flue gas heated type steam boiler this moment, switch heat pipe magnetic valve and seawater valve according to the different courses of work, realize heating desorption and cooling adsorption process.
For two generator continuous refrigeration systems, comprise that parts are two adsorbent beds, two steam generator/heat pipe bringing-up sections, two heat pipe descending brancies, two sea water condensers, two heat pipe magnetic valves, two seawater valves, a flue gas heating steam boiler, a seawater inlet, a seawer outlet.Two steam generator/heat pipe bringing-up sections are installed in the top of flue gas heating steam boiler, sea water condenser is installed in two adsorbent bed inner upper spaces respectively, the heat pipe magnetic valve is installed between the heat pipe descending branch and steam generator/heat pipe bringing-up section of adsorbent bed, the heat pipe descending branch is installed in the bottom of adsorbent bed, two seawater valves are installed in the both sides of seawater inlet, and seawer outlet is the seawer outlet of sea water condenser.
Two adsorbent bed systems can realize continuous cooling.When an adsorbent bed heating desorption, its heat pipe magnetic valve is opened, the seawater valve closing, and adsorbent bed is finished heating desorption under the heat effect of steam generator/heat pipe bringing-up section; This moment the another one adsorbent bed the heat pipe closed electromagnetic valve, seawater valve opening, adsorbent bed are finished the cooling adsorption process under the cooling effect of sea water condenser.
Heat pipe is all adopted in recovery waste heat of the present invention, cooling, and the heat exchanger that traditional adsorbent bed adopted with respect in the past simplifies the structure, simultaneously owing to adopting phase-change heat transfer, so also strengthened heat transfer property.The adsorbent bed of this structure is owing to can adopt seawater directly to cool off, so with respect to traditional be the adsorbent bed of cold-producing medium with ammonia, saved the refrigerant pump that is adopted in fresh water Intermediate Heat Exchanger and the Intermediate Heat Exchanger, simplify system architecture on the one hand, also saved consumption of electric on the other hand.With respect to existing composite alternating heat pipe adsorbent bed, this generator has adopted steam generator to come steam regenerator/heat pipe bringing-up section is heated on the one hand, avoided the etching problem in the direct heating process of flue gas so on the one hand, also guarantee simultaneously the pressure balance of inner heat-pipe working medium section of steam regenerator/heat pipe bringing-up section and adsorbent bed and heat pipe condenser section, helped the reliability of system works.With respect to existing composite alternating heat pipe adsorbent bed, being also advantageous in that of this design can utilize a steam generator that a plurality of adsorbent beds are heated, and finishes the heating desorption process of many generators.
Description of drawings
Fig. 1 structural representation of the present invention
Fig. 2 is a double bed application structure schematic diagram of the present invention
The specific embodiment
As shown in Figure 1, the present invention includes: flue gas heated type steam boiler 1, flue gas heating pipe line 2, steam generator 3, steam regenerator/heat pipe bringing-up section 4, heat pipe magnetic valve 5, heat pipe descending branch 6, heat-pipe working medium section 7, ammonia adsorption/desorption mouth 8, ammonia mass transfer pipeline 9, ammonia pipeline 10, adsorbent bed 11, adsorb unit pipe 12, adsorbent 13, sea water condenser 14, heat pipe condenser section 15, seawaterline 16, seawater valve 17, sea intake 18, seawer outlet 19, pressure control air storage chamber 20.Its connected mode is: flue gas heating pipe line 2 is positioned at the bottom of flue gas heated type steam boiler 1, the inner logical flue gas of pipe, flue gas heating pipe line 2 space outerpaces constitute steam generator 3, employing water is medium, steam regenerator/heat pipe bringing-up section 4 bottoms link to each other with heat pipe descending branch 6 by heat pipe magnetic valve 5, insert the upper space of flue gas heating pipe line 2 in the flue gas heated type steam boiler 1 then, top by flue gas heating steam boiler 1 picks out again, inserts the inner space at adsorbent bed 11 middle parts at last again by the outer wall of adsorbent bed 11.Heat pipe magnetic valve 5 is connected between the heat pipe descending branch 6 and steam regenerator/heat pipe bringing-up section 4 of adsorbent bed bottom, heat pipe descending branch 6 is connected the bottom of adsorbent bed 11, be connected with the heat-pipe working medium section 7 of adsorbent bed 11 inside, adsorb unit pipe 12 is positioned at the lower space of adsorbent bed 11 inside, adopt steel pipe, ammonia mass transfer pipeline 9 is positioned at the middle part of adsorb unit pipe 12, adopt screen casing, ammonia pipeline 10 is welded on the top and bottom center of adsorb unit pipe 12, communicate with the ammonia mass transfer pipeline 9 of adsorb unit pipe 12 inside, ammonia adsorption/desorption mouth 8 is the outlet of ammonia pipeline 10 in adsorbent bed 11 outsides.Adsorbent 13 is filled within the adsorb unit pipe 12, is positioned at the space outerpace of ammonia mass transfer pipeline.Sea water condenser 14 is positioned at the upper space of adsorbent bed 11 inner adsorb unit pipes 12.Seawaterline 16 is connected with the two ends of sea water condenser 14, and sea intake 18 is connected with sea water condenser 14 by seawaterline 16 respectively with seawer outlet 19, and seawater valve 17 is connected on the seawaterline 16 at sea intake 18 places.The lower space of the outside of adsorb unit pipe 12 and sea water condenser 14 constitutes heat-pipe working medium section 7 in the adsorbent bed 11, and the space on sea water condenser 14 outsides and adsorb unit pipe 12 tops constitutes heat pipe condenser section 15 in the adsorbent bed 11.The bottom space of steam generator 3 is inserted in pressure control air storage chamber 20 bottoms, and wherein adopting water is liquid medium, and the top of water adopts nitrogen to come pressure control.
Adopt a steam generator 3 to finish the design of multibed system, the steam regenerator 4 of two or many generators all is arranged on the upper space of same flue gas heated type steam boiler 1.
As shown in Figure 2, be double bed composite alternating heat pipe generator, comprise: flue gas heating steam boiler 1, steam generator/heat pipe bringing-up section 2, heat pipe magnetic valve 3, adsorbent bed 4, sea water condenser 5, seawater valve 6, sea intake 7, seawer outlet 8, seawater valve 9, sea water condenser 10, adsorbent bed 11, heat pipe magnetic valve 12, steam generator/heat pipe bringing-up section 13.Steam generator/heat pipe bringing-up section 2,13 is installed in the upper space of flue gas heating steam boiler 1 inside, sea water condenser 5 is installed in the upper space of adsorbent bed 4 inside, heat pipe magnetic valve 3 is installed between adsorbent bed 4 bottom pipelines and the steam generator/heat pipe bringing-up section 2, adsorbent bed 4 and adsorbent bed 11 are installed in the space, both sides, top of flue gas heating steam boiler 1 outside respectively, are connected by steam generator/heat pipe bringing-up section 2,13 respectively with flue gas heating steam boiler 1.Sea intake 7 is connected with sea water condenser 5,10 by pipeline respectively with seawer outlet 8, and seawater valve 6 is installed on the pipeline between sea intake 7 and the sea water condenser 5.Sea water condenser 10 is installed in the upper space of adsorbent bed 11 inside, heat pipe magnetic valve 12 is installed between adsorbent bed 11 bottoms and the steam generator/heat pipe bringing-up section 13, sea intake 7 is connected with sea water condenser 5 by pipeline respectively with seawer outlet 8, and seawater valve 9 is installed on the pipeline between sea intake 7 and the sea water condenser 10.
Claims (5)
1, the composite alternating heat pipe generator that a kind of waste heat drives, comprise: flue gas heated type steam boiler (1), flue gas heating pipe line (2), heat pipe magnetic valve (5), heat pipe descending branch (6), heat-pipe working medium section (7), ammonia adsorption/desorption mouth (8), ammonia pipeline (10), adsorbent bed (11), adsorbent (13), sea water condenser (14), heat pipe condenser section (15), seawaterline (16), seawater valve (17), sea intake (18), seawer outlet (19), it is characterized in that also comprising: steam generator (3), steam regenerator/heat pipe bringing-up section (4), ammonia mass transfer pipeline (9), adsorb unit pipe (12), pressure control air storage chamber (20), flue gas heating pipe line (2) is positioned at the bottom of flue gas heated type steam boiler (1), flue gas heating pipe line (2) space outerpace constitutes steam generator (3), steam regenerator/heat pipe bringing-up section (4) bottom links to each other with heat pipe descending branch (6) by heat pipe magnetic valve (5), insert the upper space of the interior flue gas heating pipe line of flue gas heated type steam boiler (1) (2) then, top by flue gas heating steam boiler (1) picks out again, insert the inner space at adsorbent bed (11) middle part at last again by the outer wall of adsorbent bed (11), heat pipe magnetic valve (5) is connected between heat pipe descending branch (6) and the steam regenerator/heat pipe bringing-up section (4), heat pipe descending branch (6) is connected the bottom of adsorbent bed (11), be connected with plumber's matter section (7), adsorb unit pipe (12) is positioned at the inner lower space of adsorbent bed (11), ammonia mass transfer pipeline (9) is positioned at the middle part of adsorb unit pipe (12), ammonia pipeline (10) is welded on the top and bottom center of adsorb unit pipe (12), communicate with ammonia mass transfer pipeline (9), ammonia adsorption/desorption mouth (8) is that ammonia pipeline (10) is in the outside outlet of adsorbent bed (11), adsorbent (13) is filled within the adsorb unit pipe (12), be positioned at the space outerpace of ammonia mass transfer pipeline (9), sea water condenser (14) is positioned at the upper space of adsorb unit pipe (12), seawaterline (16) is connected with the two ends of sea water condenser (14), sea intake (18) is connected with sea water condenser (14) by seawaterline (16) respectively with seawer outlet (19), seawater valve (17) is connected on the seawaterline (16) that sea intake (18) locates, the lower space of the outside of adsorb unit pipe (12) and sea water condenser (14) constitutes heat-pipe working medium section (7), the space on sea water condenser (14) outside and adsorb unit pipe (12) top constitutes heat pipe condenser section (15) in the adsorbent bed (11), and the bottom space of steam generator (3) is inserted in pressure control air storage chamber (20) bottom.
2, the composite alternating heat pipe generator of waste heat driving according to claim 1 is characterized in that, it is medium that steam generator (3) adopts water, and adsorb unit pipe (12) adopts steel pipe, and ammonia mass transfer pipeline (9) adopts screen casing.
3, the composite alternating heat pipe generator of waste heat driving according to claim 1, it is characterized in that, heat pipe descending branch (6) is arranged on the bottom of adsorbent bed (11), heat-pipe working medium section (7), adsorb unit pipe (12) are arranged on adsorbent bed (11) inside, and ammonia mass transfer pipeline (9) is in adsorb unit pipe (12) inside.
4, the composite alternating heat pipe generator of waste heat driving according to claim 1, it is characterized in that, adopt a steam generator (3) to finish the design of multibed system, the steam regenerator (4) of two or many generators all is arranged on the upper space of same flue gas heated type steam boiler (1).
5, composite alternating heat pipe generator according to claim 1 or 4 described waste heats drivings, it is characterized in that, double bed composite alternating heat pipe generator, comprise: flue gas heating steam boiler (1), steam generator/heat pipe bringing-up section (2), heat pipe magnetic valve (3), adsorbent bed (4), sea water condenser (5), seawater valve (6), sea intake (7), seawer outlet (8), seawater valve (9), sea water condenser (10), adsorbent bed (11), heat pipe magnetic valve (12), steam generator/heat pipe bringing-up section (13), steam generator/heat pipe bringing-up section (2), (13) be arranged on the inner upper space of flue gas heating steam boiler (1), sea water condenser (5) is arranged on the inner upper space of adsorbent bed (4), heat pipe magnetic valve (3) is arranged between adsorbent bed (4) bottom pipeline and the steam generator/heat pipe bringing-up section (2), adsorbent bed (4) is separately positioned on the outside space, both sides, top of flue gas heating steam boiler (1) with adsorbent bed (11), pass through steam generator/heat pipe bringing-up section (2 respectively with flue gas heating steam boiler (1), 13) be connected, sea intake (7) and seawer outlet (8) are respectively by pipeline and sea water condenser (5,10) be connected, seawater valve (6) is arranged on the pipeline between sea intake (7) and the sea water condenser (5), sea water condenser (10) is arranged on the inner upper space of adsorbent bed (11), heat pipe magnetic valve (12) is arranged between adsorbent bed (11) bottom and the steam generator/heat pipe bringing-up section (13), sea intake (7) is connected with sea water condenser (5) by pipeline respectively with seawer outlet (8), and seawater valve (9) is arranged on the pipeline between sea intake (7) and the sea water condenser (10).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2004100182913A CN1300542C (en) | 2004-05-13 | 2004-05-13 | Waste heat driven composite alternating heat pipe generator |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2004100182913A CN1300542C (en) | 2004-05-13 | 2004-05-13 | Waste heat driven composite alternating heat pipe generator |
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| Publication Number | Publication Date |
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| CN1570535A true CN1570535A (en) | 2005-01-26 |
| CN1300542C CN1300542C (en) | 2007-02-14 |
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| Application Number | Title | Priority Date | Filing Date |
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| CNB2004100182913A Expired - Fee Related CN1300542C (en) | 2004-05-13 | 2004-05-13 | Waste heat driven composite alternating heat pipe generator |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1299087C (en) * | 2005-05-26 | 2007-02-07 | 上海交通大学 | Back heating type generator of heat pipe with composite adsorbent being adopted |
| CN103994680A (en) * | 2014-05-30 | 2014-08-20 | 中国水产科学研究院渔业机械仪器研究所 | Alternation type three-warm-area heat pipe device for adsorbent bed and adsorbent type refrigerating system |
| CN106288498A (en) * | 2016-08-19 | 2017-01-04 | 上海交通大学 | Adsorbent bed system |
| CN112902490A (en) * | 2021-02-04 | 2021-06-04 | 中国科学院理化技术研究所 | Adsorption refrigerator |
Family Cites Families (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1050927A (en) * | 1989-10-11 | 1991-04-24 | 华东工学院 | Utilize the adsorption refrigerating device of utilizing waste heat for refrigeration |
| JP3712775B2 (en) * | 1996-04-17 | 2005-11-02 | 大阪瓦斯株式会社 | Plate evaporator / absorber for absorption refrigerator |
| CN2345386Y (en) * | 1997-08-20 | 1999-10-27 | 郭洪伟 | Heat-pipe adsorption type refrigerating/heat pump device for bus |
| CN1122164C (en) * | 1999-01-13 | 2003-09-24 | 李定宇 | Dual-generator adsorption refrigerating system |
| US6170279B1 (en) * | 1999-07-28 | 2001-01-09 | Li Ding-Yu | Fisherman refrigerating device using engine exhaust |
| JP3932241B2 (en) * | 1999-11-22 | 2007-06-20 | 荏原冷熱システム株式会社 | Absorption refrigerator |
| JP2003014330A (en) * | 2001-06-28 | 2003-01-15 | Osaka Gas Co Ltd | Adsorption refrigeration machine |
| CN1200235C (en) * | 2002-09-18 | 2005-05-04 | 湖北登峰换热器股份有限公司 | Heat pipe adsorption type refrigerator |
-
2004
- 2004-05-13 CN CNB2004100182913A patent/CN1300542C/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1299087C (en) * | 2005-05-26 | 2007-02-07 | 上海交通大学 | Back heating type generator of heat pipe with composite adsorbent being adopted |
| CN103994680A (en) * | 2014-05-30 | 2014-08-20 | 中国水产科学研究院渔业机械仪器研究所 | Alternation type three-warm-area heat pipe device for adsorbent bed and adsorbent type refrigerating system |
| CN106288498A (en) * | 2016-08-19 | 2017-01-04 | 上海交通大学 | Adsorbent bed system |
| CN112902490A (en) * | 2021-02-04 | 2021-06-04 | 中国科学院理化技术研究所 | Adsorption refrigerator |
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| CN1300542C (en) | 2007-02-14 |
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Granted publication date: 20070214 Termination date: 20100513 |